solid soluble components

Abstract

A solid dissolvable composition comprising a crystallization agent, water, and a freshness benefit agent.

Description

[Technical Field]

[0001] A solid soluble composition (SDC) comprising a mesh microstructure formed from a dry sodium fatty acid carboxylate compound containing a high concentration of freshness-enhancing agent, which dissolves over a range of washing machine conditions such as temperature over different time intervals to deliver remarkable freshness to the fabric. [Background technology]

[0002] Formulating effective solid-soluble compositions presents considerable challenges. The compositions must be physically stable, temperature- and humidity-resistant, and furthermore, they must be able to dissolve in solution, leaving little to no material residue, thereby fulfilling their desired function. Solid-soluble compositions are well-known in the art and are used in several roles, including detergents, oral and body medications, disinfectants, and cleaning compositions.

[0003] Compositions useful as solid disinfectants and cleansers are well known in several contexts, namely as detergents, bleaches, etc. Dishwasher tablets are popular with consumers because they have several advantages over powder products, such as not requiring measurement, being small, and being easy to store. However, a recurring problem with dishwasher tablets is obtaining tablets that dissolve quickly when added to the washing solution without the need to flow-wrap the tablets to prevent them from crumbling during transport and storage. A further problem with tablets is that they are often formed by compression, which can damage the tablet components, such as the encapsulated active substance.

[0004] Attempts to optimize the performance of tablet technology have primarily focused on modifying the dissolution profile of the tablet. This is considered particularly important for tablets placed in machines, where they encounter water spray at the very beginning of the washing process. European Patent No. 264,701(A) describes a dishwasher tablet comprising a tableting aid consisting of anhydrous and hydrated metasilicates, anhydrous triphosphates, activated chlorine compounds, and a mixture of sodium acetate and spray-dried sodium zeolite.

[0005] In recent years, oral tablets have been manufactured by compressing tablet components under high pressure in a dry state. This is because the tablets are intended to disintegrate in the gastrointestinal tract to facilitate drug absorption, and therefore need to be physically and chemically stable from the time of tablet formation until they reach the gastrointestinal tract, requiring the tablet components to be tightly bound together by the compressive pressure. Initially, wet tablets were available, formed into tablets while wet, and then dried. However, such tablets could not dissolve quickly in the mouth because they were intended to disintegrate in the gastrointestinal tract. Furthermore, these tablets were not mechanically compressed strongly, lacked shape retention, and were not practically applicable to modern uses.

[0006] Tablets formed by compression under low compressive force dissolve more quickly than tablets formed by high compressive force. However, tablets manufactured by these methods are highly brittle. The disintegration and breakage of tablets before ingestion can lead to uncertainty regarding the dose of active ingredient per tablet. Furthermore, high brittleness also causes tablet breakage, resulting in waste during handling in the factory.

[0007] Another form of solid soluble composition is a sheet-like article; for example, sheet-like laundry detergent articles that are completely or substantially water-soluble are known in the art. Unlike liquid laundry detergents, these laundry detergent sheets contain little to no water. Furthermore, they are chemically and physically stable during shipment and storage, and have a significantly smaller physical and environmental footprint. In recent years, these sheet-like laundry detergent articles have made remarkable progress in various aspects, such as increasing the surfactant content by using polyvinyl alcohol (PVA) as the main film-forming agent and improving processing efficiency by using a rotary drum drying process. Consequently, these articles are becoming increasingly commercially available and popular among consumers.

[0008] However, such sheet-type laundry detergent articles still suffer from a severe limitation in the types of surfactants that can be used, because only a handful of surfactants (such as alkyl sulfates) can be processed to form sheets in rotary drum dryers. When other surfactants are incorporated into sheet-type laundry detergent articles, the resulting articles may exhibit undesirable properties (e.g., slow dissolution and undesirable solidification). Subsequently, because the choice of surfactants that can be used in sheet-type laundry detergent articles is thus limited, cleaning performance is poor, especially in areas where fabrics or garments are exposed to various types of stains that can only be effectively removed by different surfactants with complementary cleaning powers.

[0009] The chain length distribution used in solid soaps is balanced to achieve both hardness (i.e., solidity) and lathering. Chain lengths from vegetable oils include both saturated C12 and C14 fatty acids, as well as often several unsaturated C18:1 and C18:2 fatty acids. These compositions foam on their own (undesirable for use in washing machines) and, especially in the presence of more than 5% by weight of water, result in liquid, soft, or shapeless compositions. Fatty acids with C14 and unsaturated chain lengths are generally considered insoluble or softening and should be avoided in the solid-solubility compositions described herein. Fatty acid chain lengths from animal oils containing saturated C16 and C18 fatty acids are blended with vegetable oils to produce hard solid soaps. However, these longer-chain fatty acids are generally considered insoluble.

[0010] Conventional solid soap compositions are solid and generally blend various aliphatic sodium carboxylates with different counterions to achieve properties associated with good-performing solid soaps. For example, U.S. Patent No. 5,540,852 describes a mild-foaming solid soap containing a combination of 50% to 80% by weight of NaC14, NaC16, and NaC18, as well as a fraction of magnesium counterion soap. The presence of both very long-chain fatty acids and magnesium ions yields compositions that have a plate-like structure (i.e., are no longer fibrous) and do not completely dissolve during the washing cycle. British Patent Application No. 2243615(A) describes a β-phase solid soap containing long-chain (e.g., high potency) and unsaturated (e.g., high IV value) fatty acid sodium carboxylates that efficiently do not crystallize and result in a composition that does not completely dissolve. U.S. Patent No. 3,926,828 describes a transparent solid soap containing long-chain sodium soaps comprising NaC14, NaC16, and NaC18, triethanolamine counterions, and branched-chain fatty acids, providing a composition having a non-fibrous form that does not efficiently form crystals.

[0011] U.S. Patent Application Publication 2004 / 0097387(A1) describes a solid soap containing C8 and C10 soaps but substantially no C12 soap, and having a substantial amount of a hydrogenation solvent or water-soluble organic solvent, such as propylene glycol, and free, unneutralized fatty acids. The presence of a hydrogenation solvent and unneutralized fatty acids is known to alter the morphology of fatty acid carboxylates. The altered crystalline morphology adversely affects the solubility of the resulting microstructure of the crystalline mass. Furthermore, hydrogenation solvents are hygroscopic. Therefore, crystalline masses incorporating them readily absorb moisture from the air, making the composition tacky and sticky, which inherently makes it susceptible to supply chain instability, both of which are undesirable properties.

[0012] Conventional laundry compositions blend a wide variety of sodium fatty carboxylates to achieve properties associated with good-performing laundry solids. In International Publication 2022 / 122878(A1), a solid laundry soap composition having a substantial amount (85-90 wt%) of C14 or longer-chain soap, a high level of water, and about half fatty acids (i.e., unneutralized), results in non-fibrous acid soap crystals and a composition that does not dissolve completely. U.S. Patent Application Publication 2007 / 0293412(A1) describes a powder soap composition containing a combination of NaC12, NaC14, and NaC16 fatty acid sodium carboxylates and potassium counterions, wherein the extra-long-chain fatty acids result in a composition that does not dissolve completely during the wash cycle, and the potassium ions result in a crystallizer having a plate structure (i.e., no longer fibrous).

[0013] Furthermore, U.S. Patent No. 11,499,123(B2) and U.S. Patent Application Publication No. 2023 / 0037154(A1) describe various water-soluble pellets containing vegetable soap (e.g., coconut soap), freshness activators, and other components to facilitate preparation by extruder processes. For example, the main microstructures present in Example 1 of both specifications are primarily thin-layer sheets and thin-layer-like vesicle structures (Figures 1A and 1B). When vegetable soap is prepared as described herein using methods common to vegetable soap production, multiple phases consistent with conventional soap boiling are obtained (R. G. Laughlin, The Aqueous Phase Behavior of Surfactants, Academic Press, 1994, section 14.4). The presence of thin-layer sheets and thin-layer-like vesicle microstructures has numerous adverse effects on the final composition, including the production of easily deformable soft compositions and high-density pellets. These compositions also exhibit other unacceptable properties, such as susceptibility to humidity.

[0014] Finally, there are compositions designed to be stable in the presence of a considerable amount of water. For example, U.S. Patent Application Publication 2021 / 0315783(A1) describes a composition having NaC14, NaC16, and NaC18 fatty acid carboxylates, wherein the crystallizing agent forms a network that releases water when compressed. U.S. Patent Application Publication 2002 / 0160088(A1) describes C6-C30 aliphatic metal carboxylates that form a fibrous network in the presence of water and seawater to absorb oil. U.S. Patent Application Publication 2021 / 0315784(A1) describes the use of long-chain (C13-C20) sodium carboxylate fatty acids to prepare a composition that squeezes water out when compressed. These compositions require the use of fatty acids with longer chain lengths (i.e., non-water soluble). [Prior art documents] [Patent Documents]

[0015] [Patent Document 1] European Patent No. 264,701 (A) [Patent Document 2] U.S. Patent No. 5,540,852 [Patent Document 3] British Patent Application No. 2243615 (A) [Patent Document 4] U.S. Patent No. 3,926,828 [Patent Document 5] U.S. Patent Application Publication No. 2004 / 0097387 (A1) [Patent Document 6] International Publication No. 2022 / 122878 (A1) [Patent Document 7] U.S. Patent Application Publication No. 2007 / 0293412 (A1) [Patent Document 8] U.S. Patent No. 11,499,123 (B2) [Patent Document 9] U.S. Patent Application Publication No. 2023 / 0037154 (A1)[[ID=3�]] [Patent Document 10] U.S. Patent Application Publication No. 2021 / 0315783 (A1) [Patent Document 11] U.S. Patent Application Publication No. 2002 / 0160088 (A1) [Patent Document 12] U.S. Patent Application Publication No. 2021 / 0315784 (A1) [Non-Patent Document]

[0016] [Non-Patent Document 1] R.G. Laughlin, The Aqueous Phase Behavior of Surfactants, Academic Press, 1994, section 14.4 [Summary of the Invention] [[ID=5५]][Problems to be Solved by the Invention]

[0017] What is needed is a solid composition that overcomes the shortcomings of conventional technologies, can contain high levels of active substances, dissolves easily, is resistant to temperature and humidity, and enables supply chain stability. [Means for solving the problem]

[0018] A solid-soluble composition is provided, comprising a crystallizing agent, water, and a freshness-enhancing agent, wherein the crystallizing agent is a sodium salt of a saturated fatty acid having 8 to about 12 methylene groups, and the freshness-enhancing agent is at least one of a neat fragrance or an odor neutralizer.

[0019] The Solid-Soluble Composition (SDC) contains a crystallizing agent and a high concentration of freshness-enhancing agent. The composition and microstructure enable a dissolution rate of over 5% (1 min) at a dissolution temperature of 37°C, more preferably over 5% (1 min) at a dissolution temperature of 25°C, as determined by a dissolution test method for the desired dissolution profile under washing conditions. The composition and microstructure allow for very high fill densities of fragrance capsules and neat fragrances, resulting in a remarkable freshness on fabrics compared to current market products. The Solid-Soluble Composition has a low fill density, is porous, enhances dissolution, and results in enhanced, very lightweight products for e-commerce. The composition is also composed of natural, readily available, relatively inexpensive, and sustainable materials that are resistant to humidity and high temperatures to enhance stability in the supply chain.

[0020] A method for producing a solid soluble composition is provided, comprising: providing at least one of neat fragrances or odor neutralizers; mixing a solid soluble composition mixture by solubilizing a crystallizing agent in water; forming the solid soluble composition mixture by converting and maintaining it to a desired shape and size by at least one of crystallization, partial drying, salting, or viscosity increase from liquid crystal formation; and drying by removing water to produce the solid soluble composition.

[0021] A method for producing a solid soluble composition is provided, comprising: solubilizing a crystallizer in a solid soluble composition mixture (SDCM) by heating the crystallizer and the aqueous phase until the crystallizer is solubilized; optionally adding a freshness beneficial agent, often when partially cooled (i.e., mixing); in one embodiment, forming a rheological solid composition (RSC) by further cooling the solid soluble composition mixture to below the crystallization temperature to crystallize the crystallizer (i.e., forming); and producing a solid soluble composition (SDC) by removing water and adding an optional freshness beneficial agent (i.e., drying).

[0022] Fragrance capsules can be added when the mixture is cooled (i.e., mixed) without applying compressive and shear stresses, otherwise the compressive and shear stresses would break the capsule walls and release the fragrance. The fragrance can be optionally added by emulsification during the mixing stage, where fragrance droplets are stabilized by utilizing the surfactant properties of the crystallizing agent before the formation of the fibrous microstructure of the initially formed rheological solid, or it can be optionally added after the drying stage and the formation of the solid-soluble composition to allow for uniform penetration into the fibrous microstructure. [Brief explanation of the drawing]

[0023] This specification concludes with claims that describe in detail and explicitly claim the subject matter to be considered as the disclosure, but a deeper understanding of the disclosure can be gained by reading the following explanatory text in conjunction with the accompanying drawings. Some drawings have been simplified by omitting selected elements for the purpose of more clearly illustrating other elements. Such omission of elements in some drawings does not necessarily indicate the presence or absence of elements in any of the exemplary embodiments, unless explicitly stated in the corresponding written description. None of the drawings are necessarily to a certain scale. [Figure 1A] Representative scanning electron microscope (SEM) images of the microstructure of comparative examples prepared from coconut oil are shown. [Figure 1B] Representative scanning electron microscope (SEM) images of the microstructure of comparative examples prepared from hydrogenated coconut oil are shown. [Figure 2A] This image shows a scanning electron microscope (SEM) photograph of the crystallizing agent crystals in the composition of the present invention. [Figure 2B] This image shows a scanning electron microscope (SEM) of a mesh microstructure prepared from a crystallized crystallizing agent in the DSC domain of the composition of the present invention. [Figure 3A] This image shows a scanning electron microscope (SEM) of a viable fragrance capsule dispersed in a mesh microstructure of DSC domains in Example CB of the present invention, which has a PMC capsule. [Figure 3B] This image shows a scanning electron microscope (SEM) of fragrance capsules dispersed in a mesh microstructure of SDC domains in Example CB of the present invention, which has PMC capsules. [Figure 4] This image shows a scanning electron microscope (SEM) of a flavor capsule that was destroyed as a result of the pressure used to manufacture conventional compressed tablets. [Figure 5A] The image shows a microcomputed tomography (micro-CT) image of the SDC of the present invention, prepared through the process described, leaving a composition with many open pores (black and gray areas) in its microstructure to facilitate dissolution. [Figure 5B] This image shows a microcomputed tomography (micro-CT) scan of a conventional compressed tablet with a complete solid structure. [Figure 6] This graph shows the amount of fragrance in the headspace of a dry, rubbed fabric treated with a viable amount of a commercially available product (approximately 1 gram of fragrance capsule, a heaping cap) and the composition of the present invention (approximately 2.5 grams of fragrance capsule, half a cap) (e.g., similar to sample EO). The composition of the present invention has a much larger amount of fragrance in the air, and a much smaller amount of the product is added to the wash. [Figure 7A] The dissolution behavior of SDC prepared using different combinations of crystallizing agents in commercially available PEG at 37°C, 25°C, and 5°C, respectively, as determined using a dissolution test method, is shown. [Figure 7B] The dissolution behavior of SDC prepared using different combinations of crystallizing agents in commercially available PEG at 37°C, 25°C, and 5°C, respectively, as determined using a dissolution test method, is shown. [Figure 7C] The dissolution behavior of SDC prepared using different combinations of crystallizing agents in commercially available PEG at 37°C, 25°C, and 5°C, respectively, as determined using a dissolution test method, is shown. [Figure 8] This graph shows the measured stable temperatures of the SDC domain for three compositions of the present invention, using a thermal stability test method. [Figure 9] This graph shows the hydration stability of the SDC domain of the present invention (%dm < 5% at 80% RH) by measuring the water uptake at 25°C when exposed to different relative humidities using a humidity test method. This is in contrast to Comparative Example EC30, a commercially available facial cleanser, and Example 1 of U.S. Patent No. 11,499,123(B2). [Figure 10] This graph shows the dissolution profiles at 25°C, determined by a dissolution test method, as a function of the weight % of the fragrance capsules for four compositions of the present invention (Sample AA, Sample AB, Sample AC, and Sample AD). It demonstrates that the dissolution characteristics are mainly a function of the blend of crystallizing agents and do not depend significantly on the amount of fragrance capsules. [Figure 11] This graph shows the average percentage of mass loss obtained by the dissolution test method for sample AC when dissolved for 1 minute, 2 minutes, 3 minutes, and 4 minutes, respectively. The linearity of the average percentage of mass loss allows for extrapolation to complete the average mass loss up to approximately 13 minutes. [Figure 12] This graph shows the effect of SDCM composition on the possibility of crystallization during the formation stage using a mixture of C12 / C10 crystallizing agents. [Figure 13A] A representative scanning electron microscope (SEM) image of a comparative composition prepared from potassium palmitate (KC16) and exhibiting small plate-like crystals is shown. [Figure 13B]A representative scanning electron microscope (SEM) image of a comparative composition prepared from triethanolamine palmitate (TEA C16) and exhibiting small plate-like crystals is shown. [Modes for carrying out the invention]

[0024] The present invention includes a solid-soluble composition comprising a crystalline mesh. The crystalline mesh ("mesh") comprises a relatively rigid three-dimensional linked crystalline framework of fibrous crystalline particles formed from a crystallizing agent. The solid-soluble composition of the present invention has a crystallizing agent(s), a low water content, a freshness-enhancing agent(s), and is readily soluble in water at or above / below room temperature.

[0025] While not limited to theory, the counterions in the fatty acid compositions of the present invention are thought to contribute to providing the unique performance characteristics of the disclosed compositions, which will be described in more detail below. Sodium counterions result in fibrous crystals of fatty acid carboxylates that form a mesh microstructure. This mesh microstructure provides further advantages for low-density compositions, which are advantageous in ensuring rapid dissolution and reducing transport costs. Together with other counterions such as potassium, magnesium, and triethanolamine, fatty acid carboxylates form plate-like crystals, making dry compositions containing them brittle or difficult to dissolve. Counterions for non-performance solid-solubility compositions can be introduced through the use of strong alkaline agents other than sodium hydroxide (e.g., potassium hydroxide) or separately as additive salts such as potassium chloride or magnesium chloride. The use of counterions other than sodium generally does not produce the mesh structure that provides the performance characteristics of the disclosed compositions.

[0026] The disclosed solid soluble composition of the present invention contains sodium low-chain (C8-C12) fatty acid carboxylates.

[0027] The present invention may be more readily understood by referring to the detailed description of the following exemplary compositions. It should be understood that the claims are not limited to the specific products, methods, conditions, apparatus, or parameters described herein, and that the terms used herein are not intended to limit the claimed invention.

[0028] As used herein, “Solid Solubility Composition” (SDC) comprises a crystallizing agent of sodium fatty acid carboxylate, which, when processed as described herein, forms an interconnected crystalline mesh of fibers that readily dissolves at a target washing temperature; an optional freshness beneficial agent; and water in an amount of 10% by weight or less. SDC may be in solid form, such as powder, particles, aggregates, flakes, granules, pellets, tablets, lozenges, packs, briquettes, bricks, solid blocks, unit doses, or other solid forms known to those skilled in the art. In this specification, “Beads” refers to a specific solid form having a hemispherical shape with a radius of approximately 2.5 mm.

[0029] When used herein, “Solid Solubility Composition Mixture” (SDCM) comprises components of the solid solubility composition before water removal (e.g., during the mixing or crystallization stage). The SDCM comprises an aqueous phase and further comprises an aqueous support. The aqueous support may be distilled water, deionized water, or tap water. The aqueous support may be present in an amount of about 65% to 99.5% by weight, or about 65% to 90% by weight, or about 70% to 85% by weight, or about 75% by weight of the SDCM.

[0030] As used herein, “rheological solid composition” (RSC) describes the solid form of SDCM after crystallization (crystallization stage) before water removal to obtain SDC, where RSC contains more than approximately 65% ​​by weight of water, and the solid form is derived from a linked “structured” mesh (mesh microstructure) of fibrous crystalline particles from the crystallizing agent.

[0031] The “freshness enhancers” used herein and further described below include materials added to SDCM, RSC, or SDC to impart a freshness effect to fabrics through washing. In some embodiments, the freshness enhancer may be a neat fragrance. In embodiments, the freshness enhancer may be an encapsulated fragrance (fragrance capsule). In embodiments, the freshness enhancer may be a mixture of fragrances and / or fragrance capsules.

[0032] As used herein, “crystallization temperature” is used to describe the temperature at which a crystallizing agent (or combination of crystallizing agents) is completely solubilized in SDCM, or, as used herein, to describe the temperature at which a crystallizing agent (or combination of crystallizing agents) exhibits any crystallization in SDCM.

[0033] As used herein, “dissolution temperature” is used to describe the temperature at which SDC is completely solubilized in water under normal washing conditions.

[0034] As used herein, “stable temperature” is the temperature at which most (or all) of the SDC material is completely melted, such that the composition no longer exhibits a stable solid structure and can be considered a liquid or paste, and the solid soluble composition no longer functions as intended. The stable temperature is the lowest thermal transition temperature determined by a thermal stability test method. In embodiments of the present invention, the stable temperature may be greater than about 40°C, more preferably greater than about 50°C, more preferably greater than about 60°C, and most preferably greater than about 70°C, in order to ensure stability in the supply chain. Those skilled in the art will understand how to measure the lowest thermal transition temperature using differential scanning calorimetry (DSC) equipment.

[0035] As used herein, “humidity stability” is the relative humidity at which a low-moisture composition spontaneously absorbs more than 5% by weight of its original mass in water from the ambient humidity at 25°C. Absorbing small amounts of water when exposed to a humid environment allows for more sustainable packaging. Absorbing large amounts of water risks the composition softening or liquefying and no longer functioning as intended. In embodiments of the present invention, humidity stability may be greater than 70% RH, more preferably greater than 80% RH, more preferably greater than 90% RH, and most preferably greater than 95% RH. Those skilled in the art will understand the method of measuring a 5% weight increase using dynamic vapor sorption (DVS) equipment, which is further described in the humidity test methods.

[0036] When used herein, “cleaning composition” means, unless otherwise specified, general-purpose or “strong” cleaning agents in the form of granules or powders, in particular cleaning detergents; general-purpose cleaning agents in the form of liquids, gels or pastes, in particular so-called strong liquid types; liquid detergents for delicate fabrics; dishwashing detergents or light dishwashing detergents, in particular highly foaming types; dishwasher detergents, liquid detergents and disinfectants (including antimicrobial handwashing types, cleaning bars, mouthwashes, denture cleaners, toothpastes, car or carpet shampoos, and bathroom cleaners), including various pouches, tablets, granules, liquids and quick-rinsing types for household and commercial use; hair shampoos and hair conditioners; shower gels and foam baths, and metal cleaners; in addition, cleaning aids such as bleaching additives and “stain sticks” or pre-treatment types, dryer additive sheets, dry and wet wipes and pads, nonwoven fabric substrates, and products having substrates such as sponges; in addition, sprays and mists.

[0037] As used herein, “dissolves during normal use” means that a solid-soluble composition dissolves completely or substantially during a washing cycle. Those skilled in the art will recognize that washing cycles have a wide range of conditions (e.g., cycle time, machine type, washing solution composition, temperature). A suitable composition dissolves completely or substantially under at least one of these conditions. Suitable compositions and microstructures exhibit a dissolution rate of more than 5% at a dissolution temperature of 37°C, as determined by a dissolution test method, for the desired dissolution profile under washing conditions. A A more preferable dissolution temperature of 25°C yields a dissolution rate of over 5% M A This makes it possible.

[0038] As used herein, the term "bio-based" material refers to renewable materials.

[0039] As used herein, the term “renewable material” refers to a material produced from a renewable material. As used herein, the term “renewable resource” refers to a resource produced by natural processes at a rate comparable to its consumption rate (e.g., within a 100-year timeframe). This resource may be replenished naturally or by agricultural technology. Non-limiting examples of renewable resources include plants (e.g., sugarcane, beets, maize, potatoes, citrus fruits, woody plants, lignocellulose, hemicellulose, and cellulose waste), animals, fish, bacteria, fungi, and forest products. These resources may be naturally occurring, hybridized, or genetically modified organisms. Natural resources such as crude oil, coal, natural gas, and peat, which take more than 100 years to form, are not considered renewable resources. Since at least a portion of the materials of the present invention are derived from renewable resources that can be decarbonized, the use of these materials can reduce the potential for global warming and fossil fuel consumption.

[0040] As used herein, the term “bio-based content” refers to the amount of carbon in a material derived from renewable resources, as a percentage of the weight (mass) of the total organic carbon in the material, determined using ASTM D6866-10, Method B.

[0041] The term "solid" refers to the physical state of a composition under the expected conditions for storage and use of a solid-soluble composition.

[0042] When used herein, articles such as "a" and "an" are understood to mean one or more of the claims or descriptions when used in the claims.

[0043] As used herein, the terms “include,” “includes,” and “including” are intended to be non-limiting.

[0044] Unless otherwise noted, all concentrations of components or compositions refer to the active portion of that component or composition, excluding impurities that may be present in the commercially available source of such components or compositions, such as residual solvents or by-products.

[0045] All percentages and ratios are calculated on a weight basis unless otherwise specified. All percentages and ratios are calculated based on the total composition unless otherwise specified.

[0046] It should be understood that all maximum numerical limits given throughout this specification include all lower numerical limits as if they were explicitly stated herein. All minimum numerical limits shown throughout this specification include all higher numerical limits as if they were explicitly stated herein. All numerical ranges given throughout this specification include all narrow numerical ranges that fall within such broad numerical ranges as if they were explicitly stated herein.

[0047] The solid soluble composition (SDC) comprises fibrous linked crystals (Figures 2A and 2B) having sufficient crystalline fiber length and concentration to form a mesh microstructure. The mesh allows the SDC to be solid with a relatively small amount of material. The mesh also allows for the capture and protection of particulate activators, such as freshness beneficial agents, such as fragrance capsules (Figures 3A and 3B). In some embodiments, the activator, e.g., freshness beneficial activator, may be discrete particles having a diameter of less than 100 μms, preferably less than 50 μms, and more preferably less than 25 μms, such as fragrance capsules. Furthermore, the activator, e.g., freshness beneficial agent, may be a liquid freshness beneficial agent, such as neat fragrance. The voids in the mesh microstructure allow for the inclusion of very high concentrations of activator. In embodiments, preferably up to about 15% by weight, preferably up to about 15% to about 0.01% by weight, preferably about 15% to about 0.5% by weight, preferably about 15% to about 2% by weight, and most preferably about 15% to about 2% by weight of activator can be added. The voids also provide pathways for water to be incorporated into the microstructure during washing, accelerating dissolution compared to a completely solid composition.

[0048] Remarkably, it is possible to prepare SDCs with high solubility, low water content, moisture resistance, and thermal stability. Sodium salts of long-chain fatty acids (i.e., sodium myristate (NaC14) to sodium stearate (NaC18)) can form fibrous crystals. It is generally understood that the crystal growth pattern resulting in fibrous crystallization reflects the hydrophilic (head group) and hydrophobic (hydrocarbon chain) balance of the NaC14-NaC18 molecules. As disclosed in this application, the crystallizers used have the same hydrophilic contribution but exhibit very different hydrophobicity due to the shorter hydrocarbon chain of the fatty acid sodium carboxylate used. In fact, the carbon chain is about half the length of those previously disclosed (US Patent Application Publication 2021 / 0315783). Furthermore, those skilled in the art will recognize that many surfactants, such as ethoxylated alcohols with the same chain but different head groups, are susceptible to considerable moisture incorporation and significant temperature-induced changes. The selected group of crystallizers in the present invention enables all of these desirable properties.

[0049] Methods for producing solid-soluble compositions offer several advantages over other approaches. Firstly, as previously mentioned, producing similar compositions by compression (e.g., tablet making) and, in some cases, extrusion, has detrimental effects on dispersed flavor capsules. The tablet-making process compresses the solid material, and although not desired to be bound by theory, it introduces significant local strain into the material, rupturing the flavor capsules and releasing the encapsulated flavor (Figure 4). Secondly, the production of similar compositions by compression (e.g., tablet making) also compresses the structure, making them denser and less soluble (Figures 5A and 5B). Thirdly, the main commercially available fabric freshness bead production processes limit the selection of freshness beneficial agents. Polyethylene glycol (PEG), used to form most currently commercially available beads, must be processed at temperatures between 70°C and 80°C, which is higher than the melting point of PEG. Preparing SDC at approximately 25°C allows for a wider variety of neat flavors and flavor capsules. In actual processes, the melting point temperature of PEG must be maintained for several hours, and some fragrance ingredients are highly volatile and evaporate during processing. Inclusion of fragrance oils for SDC is carried out at room temperature, thus broadening the range of fragrance ingredients that can be added as neat fragrances. Finally, many fragrance capsule wall chemistrys cease to function at higher process temperatures, causing the fragrance to release prematurely and thus becoming ineffective as freshness-beneficial activators. By enabling lower temperature process conditions, the SDC compositions described herein allow for the utilization of a wider range of capsule wall chemistrys.

[0050] Currently available water-soluble polymers limit the use of fragrance capsules as fragrance enhancer delivery systems. Fragrance capsules are delivered in aqueous slurry, with the slurry limited to a maximum of 20-30% by weight of the encapsulated fragrance, and the total amount of encapsulated fragrance limited to approximately 1.2% by weight. The use of fragrance capsule concentrations exceeding these is limited by the active concentration in the fragrance capsule slurry, which also introduces water that prevents the water-soluble carrier from solidifying, thereby limiting fragrance capsule delivery. As a result, consumers generally do not fully enjoy the desired amount of freshness due to limitations on what they can add to their cleaning solutions. The solid-soluble composition of the present invention can construct fragrance capsules exceeding 15% by weight, resulting in approximately 10 times greater freshness delivery compared to current water-soluble polymers. Such high delivery is at least partially enabled by the low water content of the composition, allowing users to experience a significant freshness upgrade over current commercially available fabric freshness beads (Figure 6).

[0051] The improved performance of the present invention's composition compared to current freshness laundry beads is thought to be related to the solubility of the composition's matrix. While not limited to theory, if the composition dissolves in the later stages of the wash cycle, the fragrance capsules are likely to remain on the fabric throughout the wash cycle (TTW), enhancing freshness performance. Optimizing performance is complicated by the wide variety of wash conditions worldwide. For example, Japan uses cold water at 4°C, North America uses 25°C, and Russia uses 37°C. Furthermore, North America can utilize top-loading machines with large amounts of water. In much of the world, highly efficient machines with much less water are used, which can make complete dissolution a problem. Current water-soluble polymers used in commercially available fabric freshness beads have limited solubility, set by the limited molecular weight range of polyethylene glycol (PEG) used as the solubility matrix. Consequently, a single PEG bead must function under a range of machine and wash conditions, limiting performance. The solubility of this composition can be adjusted to suit a range of machine and wash conditions by adjusting the ratio of the composition components (e.g., sodium laurate (nAl):sodium decanoate (NaD) ratio). (Figures 7A-7C) This allows for the creation of a wide range of compositions useful under many different washing conditions, with various SDCs releasing freshness beneficial agents at different times during the washing cycle. Figure 7A - Different time profiles at 37°C, Figure 7B - Different time profiles at 25°C, and Figure 7C - Different profiles at 4°C for commercially available PEG-based beads.

[0052] Controlling water migration in mixed bead compositions (e.g., low-water-content and high-water-content beads) is difficult with current water-soluble polymers because water migrates to the surface of the high-water-content beads. Since beads are often packaged in encapsulated packages to minimize moisture permeation into and out of the package, moisture trapped on the surface of the high-water-content beads comes into contact with the surface of the low-water-content beads, leading to bead aggregation and product distribution problems. In contrast, the structure of solid-soluble compositions prevents water migration from the SDC and therefore allows the use of water-sensitive materials (e.g., cationic polymers, bleaches).

[0053] As mentioned above, current bead formulations using PEG (and other structured materials) are prone to decomposition when exposed to heat and / or humidity during transport. Therefore, special transport conditions and / or packaging are often required to mitigate such degradation. The SDC of the present invention comprises a crystalline structure that is stable within a range of temperature and humidity conditions. In a preferred embodiment, the SDC essentially does not exhibit a melt transition below 50°C, and in a most preferred embodiment, the SDC essentially does not exhibit a melt transition below 40°C, as determined by a thermal stability test method (Figure 8). As a result, no additional resources are required for refrigeration and plastic packaging during transport to prevent moisture migration. The SDC allows for robust protection of freshness beneficial agents. In a preferred embodiment, the SDC exhibits less than 5% dm at 70% RH at 25°C, as determined by a humidity test method, in a more preferred embodiment, less than 5% dm at 80% RH, and in a most preferred embodiment, less than 5% dm at 90% RH (Figure 9).

[0054] While we do not wish to be limited to theory, it is believed that the high dissolution rate of solid-state compositions is at least partially provided by the mesh microstructure. This is considered important because this porous structure provides the product with both "lightness" and the ability to dissolve rapidly compared to compressed tablets, which allows for easy delivery of the active substance during use. It is considered important that a single crystallizer (or a combination of other crystallizers) forms fibers in the process of preparing the solid-state composition. Fiber formation enables solid-state compositions that can retain the active substance without requiring compression that could break microencapsulation.

[0055] In this embodiment, the fibrous crystals may have a minimum length of 10 μm and a thickness of 2 μm, as determined by a fiber testing method.

[0056] In the embodiment, the freshness beneficial agent may be in the form of particles, which may be a) uniformly dispersed within a mesh microstructure, b) coated on the surface of a mesh microstructure, or c) some of the particles may be dispersed within a mesh microstructure and some of the particles may be coated on the surface of a mesh microstructure. In the embodiment, the freshness beneficial agent may be a) in the form of a soluble film on the upper surface of a mesh microstructure, b) in the form of a soluble film on the bottom surface of a mesh microstructure, or c) in the form of a soluble film on both the bottom and top surfaces of the mesh. The active substance may exist as a combination of a soluble film and particles.

[0057] Crystallizing agent The crystallizing agent is selected from a small group of sodium fatty acid carboxylates having saturated chains and chain lengths in the range of C8 to C12. Within this compositional range, using the described preparation method, such sodium fatty acid carboxylates provide a fibrous mesh microstructure, an ideal solubilization temperature for preparation and use, and, by appropriate blending, the resulting solid soluble compositions can have their properties adjusted to suit various applications and conditions.

[0058] The crystallizing agent may be present in the solid soluble composition mixture in amounts of approximately 5% to approximately 50% by weight, approximately 10% to approximately 35% by weight, and approximately 15% to approximately 35% by weight. The crystallizing agent may also be present in the solid soluble composition in amounts of approximately 50% to approximately 99% by weight, approximately 60% to approximately 95% by weight, and approximately 70% to approximately 90% by weight.

[0059] Suitable crystallizing agents include sodium octanoate (NaC8), sodium decanoate (NaC10), sodium dodecanoate, or sodium laurate (NaC12), and combinations thereof.

[0060] aqueous phase The solid soluble composition mixture and the aqueous phase present in the solid soluble composition consist of an aqueous support of water and other trace components, optionally including a sodium chloride salt. The aqueous phase should contain a minimum amount of salt with other (non-sodium) cations or a hydrogen solvent.

[0061] The aqueous phase may be present in the solid soluble composition mixture in an amount of about 65% to about 95% by weight, about 65% to about 90% by weight, or about 65% to about 85% by weight of the rheological solid formed as an intermediate composition after the crystallization of the solid soluble composition mixture.

[0062] Sodium chloride in the aqueous phase solid solubility composition mixture may be present in amounts of 0% to about 10% by weight, 0% to about 5% by weight, and 0% to about 1% by weight. The most preferred embodiment contains less than 2% by weight of sodium chloride to ensure the best humidity stability.

[0063] Capsule materials The capsule may include a wall material that encloses the beneficial agent (beneficial agent delivery capsule or simply “capsule”). The beneficial agent may be referred to herein as “beneficial agent” or “encapsulated beneficial agent”. The encapsulated beneficial agent is enclosed within a core. The beneficial agent may be at least one of a fragrance mixture, an odor neutralizer, or a combination thereof. In one embodiment, the fragrance delivery technology may include beneficial agent delivery particles formed by at least partially encapsulating the beneficial agent with a wall material. The beneficial agents are 3-(4-t-butylphenyl)-2-methylpropanal, 3-(4-t-butylphenyl)-propanal, 3-(4-isopropylphenyl)-2-methylpropanal, 3-(3,4-methylenedioxyphenyl)-2-methylpropanal, and 2,6-dimethyl-5-heptenal, α-damascone, β-damascone, γ-damascone, β-damascenone, 6,7-dihydro-1,1,2,3,3-pentamethyl-4(5H)-indanone, methyl-7,3-dihydro-2H-1,5-benzodioxepin-3-one, and 2-[2-(4-methyl-3-cyclohexenyl-1-yl)propyl]cyclopenta Materials may be selected from the group consisting of fragrance raw materials such as n-2-one, 2-sec-butylcyclohexanone, and β-dihydroionone, linalool, ethyllinalool, tetrahydrolinalool, and dihydromyrcenolate; waxes such as silicone oil and polyethylene wax; essential oils such as fish oil, jasmine, camphor, and lavender; skin cooling agents such as menthol and methyl lactate; vitamins such as vitamins A and E; sunscreens; glycerin; catalysts such as manganese catalysts or bleaching catalysts; bleaching particles such as perborates; silicon dioxide particles; antiperspirant active substances; cationic polymers, and mixtures thereof. Suitable beneficial agents can be obtained from Givaudan Corp. (Mount Olive, New Jersey, USA), International Flavors & Fragrances Corp. (South Brunswick, New Jersey, USA), Firmenich Company (Geneva, Switzerland), or Encapsys Company (Wisconsin, USA).As used herein, “Fragrance raw materials” means one or more of the following: aromatic essential oils; aromatic compounds; materials supplied with aromatic essential oils, aromatic compounds, stabilizers, diluents, processing agents, and admixtures; and any materials commonly associated with aromatic essential oils and aromatic compounds.

[0064] The wall (or shell) material of the beneficial agent delivery capsule may include melamine, polyacrylamide, silicone, silica, polystyrene, polyurea, polyurethane, polyacrylate-based materials, polyacrylic acid ester-based materials, gelatin, styrene-malic anhydride, polyamide, aromatic alcohol, polyvinyl alcohol, and mixtures thereof. Melamine wall materials may include melamine crosslinked with formaldehyde, melamine-dimethoxyethanol crosslinked with formaldehyde, and mixtures thereof. Polystyrene wall materials may include polystyrene crosslinked with divinylbenzene. Polyurea wall materials may include urea crosslinked with formaldehyde, urea crosslinked with glutaraldehyde, polyisocyanates reacted with polyamide, polyamines reacted with aldehyde, and mixtures thereof. Polyacrylate-based wall materials may include polyacrylates formed from methyl methacrylate / dimethylaminomethyl methacrylate, amine acrylates and / or methacrylates, polyacrylates formed from strong acids, carboxylic acid acrylates and / or methacrylate monomers, polyacrylates formed from strong bases, amine acrylates and / or methacrylate monomers, polyacrylates formed from carboxylic acid acrylates and / or carboxylic acid methacrylate monomers, and mixtures thereof.

[0065] The composition may contain beneficial agent delivery capsules in an amount of about 0.05% to about 20% by weight, or about 0.05% to about 10% by weight, or about 0.1% to about 5% by weight, or about 0.2% to about 2% by weight of the composition. The composition may contain a sufficient amount of beneficial agent delivery capsules to provide the composition with an enclosed beneficial agent, preferably a fragrance ingredient, in an amount of about 0.05% to about 10% by weight, or about 0.1% to about 5% by weight, or about 0.1% to about 2% by weight of the composition. Where used herein, the amount or weight percentage of beneficial agent delivery capsules refers to the total of the wall material and the core material.

[0066] The group of beneficial agent delivery capsules according to this disclosure can be characterized by a volume-weighted median particle size of about 1 to about 100 microns, preferably about 10 to about 100 microns, preferably about 15 to about 50 microns, more preferably about 20 to about 40 microns, and even more preferably about 20 to about 30 microns. Different particle sizes can be obtained by controlling the droplet size during emulsification.

[0067] The beneficial drug delivery capsule may feature a core-to-shell ratio of up to 99:1, or even 99.5:1, based on weight.

[0068] Polyacrylic acid ester-based wall materials may include polyacrylic acid esters formed by alkyl and / or glycidyl esters of acrylic acid and / or methacrylic acid, polyacrylic acid esters formed by acrylic acid esters and / or methacrylic acid esters having a hydroxyl group and / or a carboxyl group and an allyl gluconamide, and mixtures thereof.

[0069] Aromatic alcohol-based wall materials may include aryloxyalkanols, arylalkanols, and oligoalkanol aryl ethers. They may also include aromatic compounds having at least one free hydroxyl group, and particularly preferably at least two directly aromatically bonded free hydroxyl groups, where the at least two free hydroxyl groups are preferably directly bonded to the aromatic ring, and more preferably at the meta position relative to each other. The aromatic alcohol is preferably selected from phenol, cresol (o-, m-, and p-cresol), naphthol (alpha- and beta-naphthol), and thymol, as well as ethylphenol, propylphenol, fluorophenol, and methoxyphenol.

[0070] The polyurea wall material may also contain polyisocyanate.

[0071] The shell of the beneficial agent delivery capsule may contain a polymer material which may be a reaction product of polyisocyanate and chitosan. The shell may also contain a polyurea resin, which contains a reaction product of polyisocyanate and chitosan. The beneficial agent delivery capsule of this disclosure may be considered a polyurea beneficial agent delivery capsule and may contain a polyurea-chitosan shell. (As used herein, "shell" and "wall" are interchangeable terms with respect to the beneficial agent delivery capsule unless otherwise indicated.) The shell may be derived from isocyanate and chitosan.

[0072] The delivery capsule may be manufactured according to a process comprising the following steps: forming an aqueous phase containing chitosan in an aqueous acidic medium; forming an oil phase comprising dissolving together at least one beneficial agent and at least one polyisocyanate; forming an emulsion by mixing the aqueous phase and the oil phase in an excess aqueous phase under high shear stirring, thereby forming droplets of the oil phase and beneficial agent dispersed in the aqueous phase; and curing the emulsion by heating for a time sufficient to form a shell at the interface between the droplets and the aqueous phase, wherein the shell contains the reaction product of the polyisocyanate and hydrolyzed chitosan, and the shell surrounds a core containing droplets of the oil phase and beneficial agent. A diluent, such as isopropyl myristate, may be used to adjust the hydrophilicity of the oil phase. The oil phase is then added to the aqueous phase and pulverized at high speed to obtain the target size. The emulsion is then cured in one or more heating steps.

[0073] The temperature and time are selected so as to be sufficient to form and cure a shell at the interface between the oil phase droplets and the water continuous phase. For example, the emulsion is heated to 85°C for 60 minutes, then held at 85°C for 360 minutes to cure the particles. The slurry is then cooled to room temperature.

[0074] The chitosan content of the shell as a weight percentage may be about 21% to about 95% of the shell. The ratio of chitosan to isocyanate monomer, oligomer, or prepolymer may be up to 1:10 by weight. The ratio of chitosan in the aqueous phase to isocyanate in the oil phase may be 21:79 to 90:10, or further 1:2 to 10:1, or further 1:1 to 7:1, based on weight. The shell may contain chitosan at a concentration of 21% by weight or more of the total shell, preferably about 21% to about 90% by weight, or further 21% to 85% by weight, or further 21% to 75% by weight, or 21% to 55% by weight.

[0075] Polyisocyanates may be aliphatic or aromatic monomers, oligomers, or prepolymers that usefully contain two or more isocyanate functional groups. Polyisocyanates can preferably be selected from the group comprising toluene diisocyanate, trimethylolpropane adducts of toluene diisocyanate and trimethylolpropane adducts of xylylene diisocyanate, methylenediphenyl isocyanate, toluene diisocyanate, tetramethylxylidene diisocyanate, naphthalene-1,5-diisocyanate, and phenylenediisocyanate.

[0076] Polyisocyanates can be selected from, for example, aromatic toluene diisocyanates and their derivatives used for wall formation for inclusion bodies, or aliphatic monomers, oligomers, or prepolymers, such as hexamethylene diisocyanates and their dimers or trimers, or 3,3,5-trimethyl-5-isocyanatomethyl-1-isocyanatocyclohexanetetramethylene diisocyanate. Polyisocyanates can also be selected from 1,3-diisocyanato-2-methylbenzene, hydrogenated MDI, bis(4-isocyanatocyclohexyl)methane, dicyclohexylmethane-4,4'-diisocyanate, and their oligomers and prepolymers. This list is illustrative and is not intended to limit the polyisocyanates useful in this disclosure.

[0077] The polyisocyanates useful in the present invention include isocyanate monomers, oligomers, or prepolymers having at least two isocyanate groups, or dimers or trimers thereof. Optimal crosslinking is This can be achieved using a polyisocyanate having at least three functional groups.

[0078] For the purposes of this disclosure, polyisocyanates are understood to encompass any polyisocyanate having at least two isocyanate groups and containing an aliphatic or aromatic moiety in the monomer, oligomer, or prepolymer. If aromatic, the aromatic moiety may include a phenyl, toluyl, xylyl, naphthyl, or diphenyl moiety, more preferably a toluyl or xylyl moiety. For the purposes of this specification, aromatic polyisocyanates may include diisocyanate derivatives such as biuret and polyisocyanurate. Polyisocyanates, in the case of aromatic polyisocyanates, may be, but are not limited to, methylenediphenyl isocyanate, toluene diisocyanate, tetramethylxylidene diisocyanate, polyisocyanurate of toluene diisocyanate (commercially available from Bayer under the trade name Desmodur® RC), trimethylolpropane adduct of toluene diisocyanate (commercially available from Bayer under the trade name Desmodur® L75), or trimethylolpropane adduct of xylylene diisocyanate (commercially available from Mitsui Chemicals under the trade name Takenate® D-110N), naphthalene-1,5-diisocyanate, and phenylene-5 diisocyanate.

[0079] Aromatic polyisocyanates are preferred. However, aliphatic polyisocyanates and blends thereof may be useful. Aliphatic polyisocyanates are understood as polyisocyanates that do not contain any aromatic moiety. Examples of aliphatic polyisocyanates include trimers of hexamethylene diisocyanate, trimers of isophorone diisocyanate, trimethylolpropane adducts of hexamethylene diisocyanate (available from Mitsui Chemicals), or biuret of hexamethylene diisocyanate (commercially available from Bayer under the trade name Desmodur® N 100).

[0080] The shell may decompose by at least 50% after 20 days (or less) when tested according to test method OECD 301B. The shell may preferably decompose by at least 60% of its mass after 60 days (or less) when tested according to test method OECD 301B. The shell may decompose by 30-100%, preferably 40-100%, 50-100%, 60-100%, or 60-95% after 60 days, preferably 50 days, more preferably 40 days, more preferably 28 days, and more preferably 14 days.

[0081] The polyvinyl alcohol-based wall material may contain crosslinked, hydrophobically modified polyvinyl alcohol, which contains a crosslinking agent comprising i) a first dextranaldehyde having a molecular weight of 2,000 to 50,000 Da, and ii) a second dextranaldehyde having a molecular weight of more than 50,000 to 2,000,000 Da.

[0082] The core of the beneficial agent delivery capsule of this disclosure may contain a partition modifier that can promote more robust shell formation. The partition modifier may be combined with the oleopropyl material of the core before the incorporation of the wall-forming monomer. The partition modifier may be present in the core at a concentration of about 5% to about 55% by weight, preferably about 10% to about 50% by weight, and more preferably about 25% to about 50% by weight of the core.

[0083] The partitioning modifier may include materials selected from the group consisting of vegetable oils, modified vegetable oils, mono-, di-, and tri-esters of C4-C24 fatty acids, isopropyl myristate, dodecanophenone, lauryl laurate, methyl behenate, methyl laurate, methyl palmitate, methyl stearate, and mixtures thereof. The partitioning modifier may preferably include isopropyl myristate, or more preferably consist of isopropyl myristate. The modified vegetable oil may be esterified and / or brominated. The modified vegetable oil may preferably include castor oil and / or soybean oil. U.S. Patent Application Publication No. 2011 / 0268802, incorporated herein by reference, describes other partitioning modifiers that may be useful in the beneficial agent delivery capsules described herein.

[0084] The fragrance delivery capsules may be coated with an adhesion aid, a cationic polymer, a nonionic polymer, anionic polymer, or a mixture thereof. Suitable polymers may be selected from the group consisting of polyvinyl formaldehyde, partially hydroxylated polyvinyl formaldehyde, polyvinylamine, polyethyleneimine, ethoxylated polyethyleneimine, polyvinyl alcohol, polyacrylate, and combinations thereof. The freshening composition may include beneficial agent delivery particles, one or more types of beneficial agent delivery capsules, for example, two types of beneficial agent delivery capsules, wherein one of the first or second beneficial agent delivery capsules has a wall made of a different wall material than the other; (b) a wall containing a different amount of wall material or monomer than the other; or (c) a different amount of fragrance oil component than the other; (d) a different fragrance oil; (e) a wall portion that is cured at a different temperature; (f) a fragrance oil having a different cLogP value; (g) a fragrance oil having a different volatility; (h) a fragrance oil having a different boiling point; (i) a wall portion made of a different weight ratio of wall material; (j) a wall portion that is cured at a different curing time; and (k) a wall portion that is heated at a different rate.

[0085] Preferably, the fragrance delivery capsule has a wall material containing an acrylic acid polymer or a derivative thereof, and a beneficial agent containing a fragrance mixture.

[0086] More preferably, the fragrance delivery capsule comprises a silica-containing wall material, such as the delivery capsule disclosed in U.S. Patent Application Publication No. 2020 / 0330949, and a beneficial agent containing a fragrance mixture.

[0087] Most preferably, the fragrance delivery capsule has a wall material containing polyisocyanate-crosslinked chitosan, as disclosed in U.S. Patent Application Publication No. 2021 / 0339217.

[0088] Neat fragrance ingredients The solid-soluble composition may contain unencapsulated fragrances that provide only a pleasurable effect (i.e., they do not neutralize malodors but provide a pleasant scent). Suitable fragrances are disclosed in U.S. Patent No. 6,248,135. For example, the solid-soluble composition may contain a mixture of volatile aldehydes for neutralizing malodors and fragrance aldehydes for providing pleasure.

[0089] Fragrances other than volatile aldehydes in the odor control components are incorporated into the solid-soluble composition.

[0090] solid soluble composition A consumer product comprising multiple particles used to refresh laundry, comprising a solid-soluble composition having one or more beneficial agents (e.g., fragrance capsules, neat fragrance) dispersed throughout the particles. In one embodiment, the freshness beneficial agent is a fragrance capsule. In another embodiment, the freshness beneficial agent is a neat fragrance. In yet another embodiment, the freshness beneficial agent is a neat fragrance in the form of dispersed droplets. In yet another embodiment, the freshness beneficial agent is a neat fragrance distributed throughout a fibrous microstructure. In yet another embodiment, one freshness beneficial agent is a fragrance capsule and a second freshness beneficial agent is a neat fragrance.

[0091] In one embodiment, the consumer product comprises SDC, which is a solid form of beads, all of which are the same solid soluble composition. In another embodiment, the solid form in the consumer product is one or more solid soluble compositions (e.g., several solid soluble compositions containing PMC, and several solid soluble compositions containing fragrances). The solid form of SDC may be powder, particles, aggregates, flakes, granules, pellets, tablets, lozenges, packs, briquettes, bricks, solid blocks, unit doses, or other solid forms known to those skilled in the art.

[0092] In one embodiment, SDC contains less than about 13% by weight. In another embodiment, SDC contains about 10% by weight and less than 1% by weight of neat flavoring. In yet another embodiment, SDC contains about 8% by weight and less than 2% by weight of neat flavoring.

[0093] In one embodiment, the SDC contains less than about 18% by weight of fragrance capsules. In another embodiment, the SDC contains about 0.01% to about 15% by weight of fragrance capsules, preferably about 0.1% to about 15% by weight, more preferably about 1% to about 15% by weight, and most preferably about 5% to about 15% by weight, based on the total weight of the solid soluble composition.

[0094] The aqueous phase may be present in the solid soluble composition in amounts of 0% to about 10% by weight, 0% to about 9% by weight, 0% to about 8% by weight, or about 5% by weight of the intermediate rheological solid.

[0095] In one embodiment, the consumer product is added directly to the wash drum at the start of the wash cycle. In another embodiment, the consumer product is added to a fabric conditioner cup inside the washing machine. In yet another embodiment, the consumer product is added at the start of the wash cycle. In yet another embodiment, the consumer product is added during the wash cycle.

[0096] In one embodiment, the consumer product is sold in paper packaging; in one embodiment, the consumer product is sold in unit dose packaging; in one embodiment, the consumer product is sold in particles of different colors; in one embodiment, the consumer product is sold in small pouches; in one embodiment, the consumer product is sold in particles of different colors; in one embodiment, the consumer product is sold in a recyclable container.

[0097] Dissolution test method All samples and procedures are maintained at room temperature (25±3°C) before testing and placed in a desiccant chamber (0%RH) for 24 hours or until a constant weight is reached.

[0098] All dissolution measurements are performed at a controlled temperature and a constant stirring rate. A 600 mL jacketed beaker (Cole-Palmer, catalog no. UX-03773-30, or equivalent) is mounted and cooled to the desired temperature by circulating water through the jacketed beaker using a water circulator (Fisherbrand Isotemp 4100, or equivalent) set to the desired temperature. The jacketed beaker is placed in the center of the stirring element of a VWR Multi-Position Stirrer (VWR North American, West Chester, PA, USA catalog no. 12621-046). 100 mL of deionized water (MODEL 18MΩ, or equivalent) and a stirring rod (VWR, Spinbar, catalog no. 58947-106, or equivalent) are added to a second 150 mL beaker (VWR North American, West Chester, PA, USA catalog no. 58948-138, or equivalent). Place the second beaker into the jacketed beaker. Add enough Millipore water to the jacketed beaker so that the water level in the jacketed beaker is higher than that in the second beaker, taking great care to prevent the water in the jacketed beaker from mixing with the water in the second beaker. Set the stirring rod speed to 200 RPM, sufficient to generate a gentle vortex. The temperature is set to reach 25°C or 37°C in the second beaker using the flow from the water circulator, and the relevant temperature is reported in the example. Before conducting the dissolution experiment, measure the temperature in the second beaker with a thermometer.

[0099] All samples were sealed in a desiccator prepared with a fresh desiccant (VWR, Desiccant-Anhydrous Indicating Drierite, stock number 23001, or equivalent) until a certain weight was reached. All test samples had a mass of less than 15 mg.

[0100] A single dissolution experiment is performed by removing a single sample from the desiccator. The sample is weighed within one minute of being removed from the desiccator, and its initial mass (M I) is measured. The sample is dropped into the second beaker while stirring the sample. The sample is dissolved for 1 minute. At the end of 1 minute, the sample is carefully removed from the deionized water. The sample is placed back in the desiccator until a constant final mass (M F ) is reached. The percentage of mass loss of the sample in a single experiment is M L = 100 * (M I - M F ) / M I and is calculated as.

[0101] Nine additional dissolution experiments are performed by first replacing 100 ml of water with fresh deionized water, adding a new sample from the desiccator for each experiment, and repeating the dissolution experiment described in the previous paragraph.

[0102] The average percentage of mass loss for the test (M A ) is calculated as the average percentage of mass loss for the 10 experiments, and the average standard deviation of the mass loss (SD A ) is the standard deviation of the average percentage of mass loss for the 10 experiments.

[0103] This method returns three values: 1) the average mass of the sample (M S ), 2) the temperature (T) at which the sample is dissolved, and 3) the average percentage of mass loss (M A . If the method is not executed on the sample, the method returns "NM" for all values. The average percentage of mass loss (M A ) and the average standard deviation of the average percentage of mass loss (SD A ) are used to plot the dissolution curves shared in Figures 7 and 10.

[0104] Humidity Test Method Before the test, all samples and procedures are maintained at room temperature (25 ± 3°C).

[0105] A humidity test method is used to determine the amount of water vapor sorption that occurs in the raw material or composition between drying at 0% RH and drying at various RHs at 25°C. In this method, 10–60 mg of sample is weighed, and the mass change associated with adjustment under different environmental conditions is captured using a dynamic vapor sorption instrument. The resulting mass increase is expressed as a percentage change in mass per unit of the dry sample mass recorded at 0% RH.

[0106] This method utilizes an SPSx Vapor Sorption Analyzer (ProUmid GmbH&Co.KG, Ulm, Germany) with a resolution of 1 μg, or an equivalent dynamic vapor sorbent (DVS) instrument capable of controlling relative humidity (%RH) to within ±3%, temperature to within ±2°C, and measuring mass with an accuracy of ±0.001 mg.

[0107] Disperse 10-60 mg of the raw material or composition sample uniformly in a tare-filled 1-inch diameter aluminum pan. Place the aluminum pan containing the dispersed raw material or composition sample into a DVS (Deep Vase System) apparatus, set the DVS apparatus to 25°C and 0%RH, and record the mass at that point with an accuracy of 0.001 mg or better approximately every 15 minutes. After the sample has been in the DVS under these conditions for a minimum of 12 hours and a constant weight has been achieved, record the mass of the sample m d The amount is recorded with an accuracy of 0.01 mg or higher. Once this step is complete, the instrument is advanced in 10% RH increments up to 90% RH. The sample is held in DVS for a minimum of 12 hours at each step, and the mass of the sample is measured m until a constant weight is reached. n The data is recorded with an accuracy of 0.001 mg or higher at each stage.

[0108] For a specific sample, constant weight can be defined as the change in continuous mass weighing that does not differ by more than 0.004%. For a specific sample, the change in mass % (%dm) per unit of dry sample mass is defined as follows:

[0109]

number

[0110] The percentage change in mass per unit of dry sample mass is reported in units of 0.01%.

[0111] Thermal stability test method All samples and procedures are maintained at room temperature (25±3°C) and at a relative humidity of 40±10% for 24 hours prior to testing.

[0112] In the thermal stability test method, differential scanning calorimetry (DSC) is performed on a 20 mg ± 10 mg sample of the sample composition. Simple scanning is performed between 25°C and 90°C, and the temperature at which the maximum peak is observed is considered the stable temperature and reported in the nearest °C.

[0113] The sample is filled into the DSC dish. All measurements are performed using a high-volume stainless steel dish set (TA part number 900825.902). The dish, lid, and gasket are weighed using a Mettler Toledo MT5 analytical microbalance (or equivalent, Mettler Toledo, LLC., Columbus, OH) to determine the tare weight. The sample is filled into the dish to a target weight of 20 mg (+ / - 10 mg) according to the manufacturer's specifications, taking care to ensure that the sample is in contact with the bottom of the dish. The dish is then sealed with a TA High Volume Die Set (TA part number 901608.905). The final assembly is weighed to obtain the weight of the sample. The sample is filled into a TA Q Series DSC (TA Instruments, New Castle, DE) according to the manufacturer's instructions. The DSC procedure uses the following settings: 1) Equilibrate at 25°C; 2) Mark the end of cycle 1; 3) Increase temperature to 90.00°C at 1.00°C / min; 4) Mark the end of cycle 3; then 5) End method; press Run.

[0114] Moisture Test Method All samples and procedures are maintained at room temperature (25±3°C) and at a relative humidity of 40±10% for 24 hours prior to testing.

[0115] The moisture content test method is used to quantify the weight percentage of water in a composition. In this method, Karl Fischer (KF) titration is performed on each of three similar samples of the sample composition. The titration is performed using a volumetric KF titrator and a one-component solvent system. The sample is 0.3 ± 0.05 g in mass and is dissolved in the titration vessel for 2.5 minutes before titration. The average (arithmetic mean) moisture content of the three test specimen replicas is reported in units of 0.1 wt% of the sample composition.

[0116] The sample composition should be prepared at 25±3°C and 40±10.0%RH for at least 24 hours before measurement. One suitable example of the apparatus and specific procedure is as follows:

[0117] To measure the water content of the sample, a Mettler Toledo V30S Volumetric KF Titrator is used. The instrument is equipped with Honeywell Fluka Hydraanal Solvent (catalog no. 34800-1L-US) for dissolving the sample, Honeywell Fluka Hydraanal Titrant-5 (catalog no. 34801-1L-US) for titrating the sample, and three drying tubes (titration bottle, solvent bottle, and waste bottle) filled with Honeywell Fluka Hydraanal Molecular sieve 3nm (catalog no. 34241-250g) to preserve the effectiveness of the anhydrous material.

[0118] The method used to measure the samples was type "KF vol", ID "U8000", and title "KFVol 2-comp 5", each having eight lines in which the method functions.

[0119] Line 1, Title has the following selected: Type is set to Karl Fischer Titration Vol.; Compatibility is set to V10S / V20S / V30S / T5 / T7 / T9; ID is set to U8000; Title is set to KFVol 2-comp 5; Author is set to Administrator; Date and time are defined along with Modified on and Modified by when the method was created; Protection is set to no and SOP is set to None.

[0120] Line 2, Sample has two options: Sample and Concentration. When the Sample option is selected, the following fields are defined as follows: Set the number of IDs to 1. Set ID1 to -- and select Entry Type as Weight. Set Lower Limit to 0.0 g. Set Upper Limit to 5.0 g. Set Density to 1.0 g / mL. Set Correction Factor to 1.0. Set Temperature to 25.0 °C. Select Auto Start and Set Entry as After Addition. When the Concentration option is selected, the following fields are defined as follows: Select Titrator to KF 2-comp 5. Set Nominal Concentration to 5 mg / mL. Select Standard to Water-Standard 10.0. Select Entry Type as Weight. Set Lower Limit to 0.0 g. Set Upper Limit to 2.0 g. Set Equilibrium to 25.0 °C. Set Mixing Time to 10 seconds. Select Auto Start. Select Entry as After Addition. The lower limit of the concentration is set at 4.5 mg / mL, and the upper limit of the concentration is set at 5.6 mg / mL.

[0121] Line 3, the titration stand (KF stand), has fields defined as follows: Set the type to KF stand. Select the titration stand to KF stand. Select the drift source to online. Set the maximum starting drift to 25.0 μg / min.

[0122] Line 4, the mixing time, has a field defined as follows: Set the duration to 150 seconds.

[0123] Line 5, Titration (KF Volume)[1] has six options: Titrate, Sensor, Agitation, Pre-distribution, Control, and Termination. When the Titrate option is selected, the following fields are defined as follows: Select Titrate to KF 2-comp 5. Set Nominal concentration to 5 mg / mL and Reagent type to 2-comp. When the Sensor option is selected, the following fields are defined as follows: Set Type to Polarization. Select Sensor to DM143-SC. Set Unit to mV. Set Indicator to Voltammetry and Ipol to 24.0 μA. When the Agitation option is selected, the following fields are defined as follows: Set Speed ​​to 50%. When the Pre-distribution option is selected, the following fields are defined as follows: Select Mode to None. Set Wait Time to 0 seconds. When the Control option is selected, the following fields are defined as follows: Set Termination to 100.00 mV. Set Control Bandwidth to 400.00 mV. Set the maximum infusion rate to 3 mL / min. Set the infusion rate (minutes) to 100 μL / min and select Start successfully. When the End option is selected, the following fields are defined as follows: Select Type as Drift Stop Relative. Set Drift to 15.0 μg / min. Vmax is 15 mL; Minimum time is set to 0 seconds and maximum time is set to ∞ seconds.

[0124] Line 6, the calculation has fields defined as follows: The result type is selected as predefined. Set the result to content. Set the result unit to %. Set the expression to R1=(VEQ * CONC-TIME * Set D...). Set the constant C to 0.1. Set the decimal part to 2. Do not select result limits. Select record statistics. Do not select extra statistical functions.

[0125] Line 7, the record has fields defined as follows: Select Result No. Select Raw Result No. Select Table of Measurements No. Select Sample Data No. Select Resource Data No. Select EV No. Select Et No. Select Vt No. Select H2O-t No. Select Drift-t No. Select H2O-t&Drift-t No. Select Vt&Drift-t No. Select Method No., Select Series Data No.

[0126] Line 8, the end of the sample, has a field defined as follows: Select Open Series.

[0127] Once a method is selected, pressing Start defines the following fields: Set Type to Method. Set Method ID to U8000. Set Sample Quantity to 1. Set ID1 to -- and Sample Size to 0g. Press the Start option again. The instrument measures the maximum drift and, once steady state is reached, allows the user to select sample addition. At this point, the user adds the 3-hole adapter, removes the stopper, places the sample in the titration beaker, replaces the 3-hole adapter and stopper, and enters the sample mass in grams on the touchscreen. The reported value is the weight percentage of water in the sample. Repeat this measurement three times for each sample and report the average of the three measurements.

[0128] Fiber testing methods The fiber testing method is used to determine whether a solid dissolution composition crystallizes under process conditions and contains fiber crystals. A simple definition of fiber is "a thread or a thread-like structure or object." Fibers have a long length in only one direction (e.g., Figures 2A and 2B). This is different from other crystalline forms such as plates or lamellae that have long lengths in two or more directions (e.g., Figures 13A and 13B). Only solid dissolution compositions containing fibers are within the scope of this invention.

[0129] A sample approximately 4 mm in diameter is placed on an SEM sample shuttle and stub (Quorum Technologies, AL200077B and E7406) having a pre-coated slit containing a 1:1 mixture of Scigen Tissue Plus optimal cutting temperature (OCT) compound (Scigen 4586) and colloidal graphite (agar scientific G303E). The placed sample is plunge-frozen in a liquid nitrogen slush bath. Next, the frozen sample is inserted into a Quorum PP 3010 Tcryo prep chamber (Quorum Technologies PP3010T) or equivalent and equilibrated to -120°C before freeze-fracturing. Freeze-fracturing is performed by cutting off the top of the vitreous sample using a cryogenic built-in knife in the cryoprep chamber. Additional sublimation is performed at -90°C for 5 minutes to remove any residual ice on the sample surface. The sample is further cooled to -150°C and sputter-coated with a Pt layer that is present in the cryo-prep chamber for 60 seconds to reduce static charge.

[0130] High-resolution imaging is performed using a Hitachi Ethos NX5000 FIB-SEM (Hitachi NX5000) or an equivalent device.

[0131] To determine the fibrous morphology of the sample, imaging is performed at a magnification of 20,000x. At this magnification, individual crystals of the crystallizing agent can be observed. The magnification may be slightly adjusted to a lower or higher value until individual crystals are observed. Those skilled in the art can evaluate the longest dimension of a representative crystal in the image. If this longest dimension is about 10 times or more the other orthogonal dimensions of the crystal, these crystals are considered fibers and are within the scope of the present invention. [Examples]

[0132] The present invention relates to a solid soluble composition (SDC) comprising a mesh microstructure formed from a dry sodium fatty acid carboxylate compound containing an activator such as a high concentration of freshness-enhancing agent, which dissolves during normal use and delivers remarkable freshness to the fabric.

[0133] The examples illustrate compositions of the present invention that can often be filled with higher concentrations of freshness-enhancing agents, including fragrance capsules and neat fragrances, than currently available in commercially available products.

[0134] In summary, Example 1 shows a composition of the present invention having fragrance capsules of various concentrations, Example 2 shows a composition of the present invention having fragrances of various concentrations, Example 3 shows a composition of the present invention having various combinations of crystallizers, Example 4 shows a comparative composition having a long-chain crystallizer, Example 5 shows a composition of the present invention having a blend of fragrance capsules and neat fragrance, and Example 6 shows a composition of the present invention using sodium chloride as a processing aid for crystallization in the formation stage of the process. Example 7 shows a composition of the present invention prepared on a pilot plant scale, allowing for higher concentrations of crystallizers in the formation process, where the crystallizer is supplied as a fatty acid and neutralized during production. Finally, Example 8 shows a composition of the present invention having fragrance capsules with different capsule chemistry.

[0135] All examples are prepared using the following three manufacturing steps. 1. Mixing - The crystallizing agent is completely soluble in water. 2. Formation - The composition from the mixing step is formed to the desired SDC size and dimensions by techniques including crystallization, partial drying, salt addition, or viscosity increase. 3. Drying - The amount of water is reduced to ensure the desired performance, including solubility, hydration, and thermal stability.

[0136] The activator is generally added to the SDC during the mixing process or after the drying process.

[0137] Tables 1 to 16 provide examples of the composition and performance parameters of the SDC and comparative SDC of the present invention.

[0138] The SDCM upper section provides all amounts of materials used in the mixing to produce the Solid Solubility Composition Mixture (SDCM). Calculate the following other items: "%CA" is the weight percentage of all crystallizing agents in the SDCM.

[0139] The SDC-Central Section provides the weight corresponding to the amount in the final solid soluble composition (SDC) from which all unbound water has been removed. Calculate the following other items: "%CA" is the percentage of all crystallizing agents in the SDC. "Retardant CA%" is the percentage of the crystallizing agent that dissolves more slowly (i.e., longer chain length) if the sample contains a mixture of crystallizing agents. "Fragrance Capsules" is the percentage of fragrance capsules in the dried SDC. "Fragrance" is the percentage of neat fragrance in the dried SDC. "AA" is the total amount of fragrance capsules and neat fragrance, if both are present.

[0140] Dissolving performance - In the section below, "M S "T" and "M A This is the output of the dissolution test method. A value of "NM" means that the performance could not be measured.

[0141] material (1) Water: Millipore, Burlington, MA (18m-ohm resistance) (2) Sodium caprate (sodium octanoate, NaC8): TCI Chemicals, catalog number 00034 (3) Sodium caprate (sodium decanoate, NaC10): TCI Chemicals, catalog number D0024 (4) Sodium laurate (sodium dodecanoate, NaC12): TCI Chemicals, catalog number L0016 (5) Sodium myristate (sodium tetradecanoate, NaC14): TCI Chemicals, catalog number M0483 (6) Sodium palmitate (sodium hexadecanate, NaC16): TCI Chemicals, catalog number P00007 (7) Sodium stearate (sodium octadecanoate, NaC18): TCI Chemicals, catalog number S0031 (8) Fragrance capsule slurry: Encapsys, encapsulated fragrance #1, melamine formaldehyde wall chemical reaction, encapsulated fragrance #1 (31% active). (9) Neat Fragrance: International Flavors and Fragrances, Neat Fragrance, Catalog No. FC CLP 20 (10) Sodium Chloride: VWR BDH Chemical, Catalog No. BDH9286-500g (11) Fatty acid blend: C810L, Procter & Gamble Chemicals, Sample code: SR26399 (12) Lauric acid: Peter Cremer, Catalog No. FA-1299, Lauric acid (13) Sodium hydroxide (50% by weight solution): Fisher Scientific, catalog number SS254-4 (14) Fragrance capsule slurry: Encapssys, encapsulated fragrance #2, polyacrylate wall chemical action, 21% by weight active (15) Fragrance capsule slurry: Encapssys, encapsulated fragrance #3, polyacrylate wall with high fragrance core-to-wall ratio, 21% by weight active (16) Fragrance capsule slurry: Encapsys, polyurea wall encapsulation fragrance #4, 32% by weight active (17) Fragrance capsule slurry: Encapssys, polyacrylate wall encapsulation fragrance #5, 6.2% by weight active

[0142] (Example 1) Example 1 shows a composition of the present invention having different levels of fragrance capsules, all of which are added during mixing. Such a combination provides consumers with remarkable dry fabric freshness.

[0143] Samples AA to AL represent the compositions of the present invention that form a fibrous mesh microstructure using two combinations of sodium fatty acid carboxylate crystallizers. Samples AA to AD (Table 1) were prepared with a nAl:nAl ratio of 70:30. NaD containing a crystallizer that dissolves more slowly in the composition is more suitable for washing at higher temperatures and / or for releasing fragrance capsules in the later stages of the washing cycle. They contain 25% by weight of the crystallizer in the SDCM and 85.0 to 97.25% by weight in the final SDC composition. Samples AE to AL (Tables 2 and 3) were prepared with a nAl:nAl ratio of 60:40. NaD containing a crystallizer that does not dissolve as slowly in the composition is more suitable for washing at higher temperatures than those shown in Table 1 (Figure 7) and / or for releasing fragrance capsules in the earlier stages of the washing cycle. They contain 25% by weight of the crystallizer in the SDCM and 82.5 to 98.9% by weight in the final SDC composition. Finally, the data from Tables 2 and 3 show that dissolution is determined not by the amount of fragrance capsules in the composition, but essentially by the composition of the crystallizer (Figure 10).

[0144] Preparation of solid soluble compositions The composition was prepared as follows:

[0145] (Mixing) A 250 ml stainless steel beaker (Thermo Fischer Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The fragrance capsules were added to a cooled solution and homogenized into the composition using a Speedmixer (Flack Tek.Inc, Landrum, SC, model DAC 150.1FVZ-K) at a speed of 3000 rpm for 3 minutes. The composition was transferred to a polymer mold containing a 5 mm diameter hemispherical pattern, uniformly dispersed using a rubber baking spatula, and excess material was scraped from the top of the mold.

[0146] The mold was placed in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C for 24 hours to allow the crystallizing agent to crystallize.

[0147] If the (dried) preparation crystallized, the mold was placed in a convection oven (Yamato, DKN400, or equivalent) set to 25°C with air circulation for an additional 24 hours. The beads were then removed from the mold and collected. When measured by the moisture content test method, the beads contained less than 5% by weight of water.

[0148] [Table 1]

[0149] [Table 2]

[0150] [Table 3]

[0151] (Example 2) Example 2 illustrates a fast-dissolving composition of the present invention having different levels of neat fragrance. Such a combination provides consumers with remarkable wet fabric freshness. This example provides several approaches to adding neat fragrance to increase the fragrance filling amount.

[0152] Samples BA to BG (Tables 4 and 5) represent compositions of the present invention that form a mesh microstructure when neat fragrance is emulsified in the mixing step. Samples BA to BF are prepared by formation through crystallization of a crystallizing agent. Unexpectedly, sample BG (Table 5) does not crystallize at 4°C when more than about 12.7% by weight of fragrance is emulsified, so it is prepared by formation by partial drying of the composition. Samples BH to BK (Table 6) show that the compositions are prepared by formation by crystallization in the absence of emulsified neat fragrance, and further by drying, where the fragrance can be added later to produce a viable SDC even at fragrance levels far exceeding 15% by weight. The samples contain 25-30% by weight of crystallizing agent in the SDCM and about 29.0% to 99.0% by weight of crystallizing agent in the final SDC composition.

[0153] Preparation of solid soluble compositions Samples BA to BG were prepared as follows.

[0154] (Mixing) A 250 ml stainless steel beaker (Thermo Fischer Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. Neat fragrance was added to a cooled solution and homogenized into the composition using a Speedmixer (Flack Tek.Inc, Landrum, SC, model DAC 150.1FVZ-K) at a speed of 3000 rpm for 3 minutes. The composition was transferred to a polymer mold containing a 5 mm diameter hemispherical pattern, uniformly dispersed using a rubber baking spatula, and excess material was scraped from the top of the mold.

[0155] The mold was placed in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C for 24 hours to allow the crystallizing agent to crystallize. If the composition did not crystallize, it had to be partially dried until crystallization occurred.

[0156] If the (dried) preparation crystallized, the mold was placed in a convection oven (Yamato, DKN400, or equivalent) set to 25°C with air circulation for an additional 24 hours. The SDC was then removed from the mold and collected. The beads contained less than 5% by weight of water, as measured by the moisture content test method.

[0157] Samples BH through BK were prepared using the same procedure, except that the neat fragrance was added after the drying stage instead of being omitted during the mixing stage of preparation, and the resulting SDC was removed from the mold and recovered. In these non-limiting cases, sample BH was prepared by adding small droplets of neat fragrance three times to the flat side of the mold. Sample BI was prepared by adding small droplets of neat fragrance three times to the round side of the mold. Sample BJ was prepared by spraying / blowing a small amount of fragrance onto the mold. Finally, sample BK was prepared by brushing small droplets of neat fragrance twice onto the round side of the mold.

[0158] [Table 4]

[0159] [Table 5]

[0160] [Table 6]

[0161] (Example 3) Example 3 illustrates a composition of the present invention having different short-chain length combinations of crystallizing agents. Such combinations provide consumers with a composition that dissolves at different times during the washing cycle to optimize the freshness performance of the fabric. Fragrance and fragrance capsule activator were added after drying.

[0162] Samples CA to CD (Table 7) were prepared using only the single-chain length of the crystallizer. All four samples were prepared by mixing the crystallizer in water, but the formation of CB to CD was carried out by crystallization in a refrigerator at 4°C, while sample CA was formed by partial drying followed by formation in a refrigerator at 4°C. These compositions exhibit a wide range of different dissolutions with time and temperature, allowing for the release of active substances at different times and washing conditions in the washing cycle. The samples contain 20% to 35% by weight of the crystallizer in SDCM.

[0163] Samples CE to CO (Tables 8, 9, and 10) were prepared from blends of C10 and C12 chain length crystallizers, covering a much wider range than in Examples 1 and 2. Formation in all compositions except CO was carried out by crystallization at 4°C. Formation in sample CO was carried out by partial drying followed by crystallization at 4°C. These samples demonstrate that by carefully blending the chain lengths of the crystallizers, a very different solubility of 18.4% to 86.0% as determined by the solubility test method was achieved. The samples contain 7.0% to 35% by weight of crystallizer in SDCM.

[0164] Samples CQ to CR (Table 11) were prepared from blends of C8 and C12 chain length crystallizers, which also covered a much wider range than in Examples 1 and 2. Formation in samples CQ and CR was carried out by crystallization at 4°C. Formation in samples CS and CT was carried out by partial drying followed by crystallization at 4°C. By carefully blending the chain lengths of the crystallizers, a very different range of dissolution, from 29.4% to 45.3%, was achieved, as determined by the dissolution test method. The samples contained 15% to 35% by weight of the crystallizer in SDCM.

[0165] Preparation of solid soluble compositions The composition was prepared as follows:

[0166] (Mixing) A 250 ml stainless steel beaker (Thermo Fisher Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The composition was transferred to a polymer mold containing a 5mm diameter hemispherical pattern, dispersed evenly using a rubber baking spatula, and any excess material was scraped off from the top of the mold.

[0167] The (forming) mold was placed in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C for 24 hours to allow the crystallizing agent to crystallize. If the composition did not crystallize, it was partially dried by blowing air over it to remove some water, and then crystallized at 4°C.

[0168] If the (dried) preparation crystallized, the mold was placed in a convection oven (Yamato, DKN400, or equivalent) for an additional 24 hours. The beads were then removed from the mold and collected. When measured by a moisture content test method, the beads contained less than 5% by weight of water.

[0169] [Table 7]

[0170] [Table 8]

[0171] [Table 9]

[0172] [Table 10]

[0173] [Table 11]

[0174] (Example 4) Example 4 shows a comparative composition having a long-chain long-crystallizing agent. A fragrance and a fragrance capsule activator were added after drying. Such compositions do not completely dissolve during the washing cycle.

[0175] Samples DA to DC (Table 12) contain comparative compositions containing a long-chain long fatty acid sodium carboxylate crystallizer. Sample DA contains C14, sample DB contains C16, and sample DC contains C18. All of these compositions were formed by crystallization at 4°C.

[0176] All samples exhibited very low solubility, as measured by the dissolution test method. In fact, the average percentage of mass loss was not measured at 25°C. Repeated measurements were reported at 37°C, a temperature preferred over the one used to increase solubility, but this still only showed an average percentage of mass loss of less than 5% in each case. Ultimately, even under the most favorable conditions for solubilization, these combinations are not viable for complete dissolution during the washing cycle. Indeed, in washing tests conducted with these compositions, hundreds of insoluble particle compositions were dispersed throughout the washing machine.

[0177] Preparation of solid soluble compositions The composition was prepared as follows:

[0178] (Mixing) A 250 ml stainless steel beaker (Thermo Fisher Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The composition was transferred to a polymer mold containing a 5mm diameter hemispherical pattern, dispersed evenly using a rubber baking spatula, and any excess material was scraped off from the top of the mold.

[0179] The mold was placed in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C for 24 hours to allow the crystallizing agent to crystallize.

[0180] The (dry) mold was placed in a convection oven (Yamato, DKN400, or equivalent) for a further 24 hours. The beads were then removed from the mold and collected. When measured by a moisture content test method, the beads contained less than 5% by weight of water.

[0181] [Table 12]

[0182] (Example 5) Example 5 shows a non-limiting sample of the present invention having blends of fragrance capsules and neat fragrance at various concentrations. Such combinations provide consumers with the opportunity for overall freshness, having both dry and wet fabric freshness, within a single SDC composition.

[0183] Sample EA contains both a low concentration of fragrance and fragrance capsules. Sample EB contains a high concentration of fragrance and low concentration of fragrance capsules to enhance wet fabric freshness. Sample EC contains a low concentration of fragrance and high concentration of fragrance capsules to enhance long-term fabric freshness. Sample ED contains both a high concentration of fragrance and fragrance capsules to meet the needs of consumers seeking a highly fresh product with a fragrance. The samples contain approximately 25% by weight of crystallizing agent in SDCM.

[0184] Preparation of solid soluble compositions The composition was prepared as follows:

[0185] (Mixing) A 250 ml stainless steel beaker (Thermo Fisher Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The fragrance capsules and neat fragrance were added to a cooled solution and homogenized into a composition using a Speedmixer (Flack Tek.Inc, Landrum, SC, model DAC 150.1FVZ-K) at a speed of 2700 rpm for 3 minutes. The composition was transferred to a polymer mold containing a 5 mm diameter hemispherical pattern, uniformly dispersed using a rubber baking spatula, and excess material was scraped from the top of the mold.

[0186] The mold was placed in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C for 24 hours to allow the crystallizing agent to crystallize.

[0187] The (dry) mold was placed in a convection oven (Yamato, DKN400, or equivalent) for a further 24 hours. The beads were then removed from the mold and collected. When measured by a moisture content test method, the beads contained less than 5% by weight of water.

[0188] [Table 13]

[0189] (Example 6) Example 6 shows compositions of the present invention having different crystallizing agents, in which sodium chloride was added in the formation of SDC. In these compositions, fragrances and fragrance capsule activators were added after drying.

[0190] Sample FA contained only C8 chain lengths that were too short to be formed by crystallization at 4°C; instead, the composition was partially dried and then crystallized at 4°C. Sample FB demonstrates that the same composition can be formed directly by adding sodium chloride to the composition and then crystallizing at 4°C. Samples FC and FD exhibited the same behavior, while SDC consisted of C10 and C10 with sodium chloride, respectively.

[0191] Preparation of solid soluble compositions The composition was prepared as follows:

[0192] (Mixing) A 250 ml stainless steel beaker (Thermo Fisher Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 80°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 80°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The fragrance capsules were added to a cooled solution and homogenized into the composition using a Speedmixer (Flack Tek.Inc, Landrum, SC, model DAC 150.1FVZ-K) at a speed of 2700 rpm for 3 minutes. The composition was transferred to a polymer mold containing a 5 mm diameter hemispherical pattern, uniformly dispersed using a rubber baking spatula, and excess material was scraped from the top of the mold.

[0193] (Formation) Formation by crystallization was carried out in a mold placed for 8 hours in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C, allowing the crystallizing agent to crystallize. Formation by partial drying, followed by crystallization, was carried out in a mold after some water had been removed by blowing air, and then crystallized in the refrigerator.

[0194] If the (dried) preparation crystallized, the mold was placed in a convection oven (Yamato, DKN400, or equivalent) for an additional 8 hours. The beads were then removed from the mold and collected. When measured by the moisture content test method, the beads contained less than 5% by weight of water.

[0195] [Table 14]

[0196] (Example 7) Example 7 shows a composition of the present invention prepared on a pilot plant scale, which allows for a higher concentration of crystallizing agent in formation, where the crystallizing agent is supplied as a fatty acid and neutralized with sodium hydroxide during mixing.

[0197] Sample FE represents the composition of the present invention prepared in a single batch tank by mixing fatty acids, sodium hydroxide, and fragrance capsules, forming a single flow by crystallization, and drying under ambient conditions. Sample FF represents the composition of the present invention by combining and mixing flows from a fatty acid melting tank and a sodium hydroxide flow, then combining this with a flow of fragrance capsule slurry, forming a final single flow by crystallization, and drying under ambient conditions. Sample FG represents the composition of the present invention prepared by the same process as Sample FF, but with a crystallizing agent of 38.5% by weight, and formation is achieved by viscosity increase. The activator is added after drying. Sample FH represents the composition of the present invention prepared by the same process as Sample FF, but with a crystallizing agent of 50.5% by weight, and formation is achieved by viscosity increase, and the activator is added after drying. The samples contain approximately 26% to 50% by weight of crystallizing agent in SDCM.

[0198] In these samples, C8 and C10 originate from the fatty acid raw material (11).

[0199] [Table 15]

[0200] (Example 8) Example 8 shows a composition of the present invention having fragrance capsules with different capsule chemistry properties. The ability to prepare compositions of the present invention with different capsule chemistry properties allows for a wider variety of freshness characteristics for consumers.

[0201] Sample FI is prepared using fragrance capsules with polyacrylate walls and chemical activity. Sample FJ is prepared using fragrance capsules with walls and chemical activity. Sample FK is prepared using fragrance capsules with chitosan walls and chemical activity. Sample FL is prepared using fragrance capsules with silica walls and chemical activity.

[0202] Preparation of solid soluble compositions The composition was prepared as follows:

[0203] (Mixing) A 250 ml stainless steel beaker (Thermo Fisher Scientific, Waltham, MA) was placed on a hot plate (VWR, Radnor, PA, 7×7 CER Hotplate, catalog number NO97042-690). Water (Milli-Q Academic) and crystallizer were added to the beaker. A temperature probe was placed in the composition. An overhead mixer (IKA Works Inc, Wilmington, NC, model RW20 DMZ) and a mixing device including a 3-blade impeller design were assembled, and the impeller was placed in the composition. The heater was set to 45°C and the impeller was set to rotate at 250 rpm, and the composition was heated to 45°C until all the crystallizer was solubilized and the composition became clear. The composition was then poured into a Max100 Mid Cup, covered, and allowed to cool to 25°C. The fragrance capsules were added to a cooled solution and homogenized into the composition using a Speedmixer (Flack Tek.Inc, Landrum, SC, model DAC 150.1FVZ-K) at a speed of 2700 rpm for 3 minutes. The composition was transferred to a polymer mold containing a 5 mm diameter hemispherical pattern, uniformly dispersed using a rubber baking spatula, and excess material was scraped from the top of the mold.

[0204] (Formation) Formation by crystallization was carried out in a mold placed for 8 hours in a refrigerator (VWR Door Solid Lock F Refrigerator 115V, 76300-508, or equivalent) equilibrated at 4°C, allowing the crystallizing agent to crystallize. Formation by partial drying, followed by crystallization, was carried out in a mold after some water had been removed by blowing air, and then crystallized in the refrigerator.

[0205] If the (dried) preparation crystallized, the mold was placed in a convection oven (Yamato, DKN400, or equivalent) for an additional 8 hours. The beads were then removed from the mold and collected.

[0206] [Table 16]

[0207] The dimensions and values ​​disclosed herein should not be understood as being strictly limited to the exact numerical values ​​listed. Instead, unless otherwise specified, each such dimension is intended to mean both the listed value and the functionally equivalent range encompassing that value. For example, a dimension disclosed as "40 mm" is intended to mean "approximately 40 mm."

[0208] All documents referenced herein, including any patents or patent applications that are cross-referenced or related, and any patent applications or patents on which this application claims priority or benefit thereof, are incorporated herein by reference in their entirety unless explicitly stated to be excluded or limited. No reference to any document shall be deemed prior art to any invention disclosed or claimed herein, nor shall it be deemed to teach, suggest or disclose any such invention, either alone or in combination with any other reference. Furthermore, if any meaning or definition of a term in this document conflicts with any meaning or definition of the same term in any document incorporated by reference, the meaning or definition given to the term in this document shall apply.

[0209] While specific embodiments of the present invention have been illustrated and described, it will be apparent 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. Therefore, it is intended that all such changes and modifications within the scope of the invention be covered in the appended claims. The inventions disclosed herein are as follows: [1] Crystallizing agent and, Water and, Contains freshness-enhancing agents, The crystallizing agent is a sodium salt of a saturated fatty acid having 8 to about 12 methylene groups. A solid-soluble composition wherein the freshness-enhancing agent is at least one of a neat fragrance or an odor neutralizer. [2] The solid solubility composition according to [1], wherein the sodium salt of the saturated fatty acid of the crystallizing agent comprises 50% to 70% by weight of C12, 15% to 25% by weight of C10, and 15% to 25% by weight of C8. [3] The solid soluble composition according to [1], wherein the sodium salt of the saturated fatty acid contains 30% to 80% of a delayed crystallizing agent (% delayed CA). [4] The solid soluble composition according to any one of [1] to [3], wherein the crystallizing agent is in the form of fibers determined by a fiber testing method. [5] The solid soluble composition according to any one of [1] to [4], wherein the amount of water is less than 50% by weight of the final solid soluble composition when determined by a moisture content test method. [6] The solid soluble composition according to any one of [1] to [5], which, when determined by a dissolution test method, has a dissolution rate of more than 5% at 37°C. [7] The freshness beneficial agent is 3-(4-t-butylphenyl)-2-methylpropanal, 3-(4-t-butylphenyl)-propanal, 3-(4-isopropylphenyl)-2-methylpropanal, 3-(3,4-methylenedioxyphenyl)-2-methylpropanal, and 2,6-dimethyl-5-heptenal, α-damascone, β-damascone, γ-damascone, β-damascenone, 6,7-dihydro-1,1,2,3,3-pentamethyl-4 A solid soluble composition according to any one of [1] to [6], wherein (5H)-indanone, methyl-7,3-dihydro-2H-1,5-benzodioxepin-3-one, 2-[2-(4-methyl-3-cyclohexenyl-1-yl)propyl]cyclopentan-2-one, 2-sec-butylcyclohexanone, and at least one of β-dihydroionone, linalool, ethyllinalool, tetrahydrolinalool, dihydromyrcenol, or a mixture thereof. [8] A solid soluble composition according to any one of [1] to [7], wherein the fragrance is enclosed in a capsule having a wall and a core, and preferably the capsule wall comprises at least one of melamine, polyacrylamide, silicone, silica, polystyrene, polyurea, polyurethane, polyacrylate-based material, polyacrylate ester, gelatin, styrene malic anhydride, polyamide, aromatic alcohol, polyvinyl alcohol, or a mixture thereof, and more preferably the capsule wall comprises a reaction product of polyisocyanate and chitosan. [9] The solid soluble composition according to [8], wherein the capsule has a volume-weighted central capsule diameter of about 1 to about 100 microns, and preferably the capsule has a core-to-shell ratio of up to 99:1 based on weight.

[10] The solid soluble composition according to [8] or [9], wherein the freshness beneficial agent is a mixture of neat fragrance and fragrance capsules.

[11] The solid soluble composition according to any one of [8] to

[10] , wherein the fragrance capsule is present in an amount of about 0.01% to about 15% by weight based on the total weight of the solid soluble composition.

[12] The solid soluble composition according to any one of [1] to

[11] , wherein the sodium salt is at least one of sodium C8, sodium C10, or sodium C12.

[13] The solid soluble composition according to any one of [1] to

[12] , wherein the crystallizing agent is present in an amount of about 50% to about 99% by weight of the solid soluble composition.

[14] The solid soluble composition according to any one of [1] to

[13] , wherein the stable temperature is higher than approximately 40°C when determined by a thermal stability test method.

[15] A method for producing a solid soluble composition, a) To provide at least one of neat fragrances or odor neutralizers, b) Mixing a solid soluble composition mixture by solubilizing the crystallizing agent in water, c) Forming the solid soluble composition mixture by converting and maintaining it to a desired shape and size by at least one of crystallization, partial drying, salt addition, or viscosity increase from liquid crystal formation, d) A method for producing a solid soluble composition, comprising drying by removing water.

Claims

1. Crystallizing agent, Water and, Contains freshness-enhancing agents, The crystallizing agent is a sodium salt of a saturated fatty acid having 8 to 12 carbon atoms. The freshness-enhancing agent comprises at least one of the following: neat fragrance, fragrance capsule, and odor neutralizer. A solid soluble composition wherein the sodium salt of the saturated fatty acid in the crystallizing agent comprises 50% to 70% by weight of C12, 15% to 25% by weight of C10, and 15% to 25% by weight of C8.

2. The solid soluble composition according to claim 1, wherein the sodium salt of the saturated fatty acid contains 30% to 80% of a delayed crystallizing agent (% delayed CA).

3. The solid soluble composition according to claim 1, wherein the crystallizing agent is the form of a fiber determined by a fiber testing method.

4. The solid soluble composition according to claim 1, wherein the amount of water is less than 50% by weight of the solid soluble composition when determined by a moisture content test method.

5. The solid soluble composition according to claim 1, wherein, when determined by a dissolution test method, the solid soluble composition has a dissolution rate of more than 5% at 37°C.

6. The aforementioned freshness-enhancing agents include 3-(4-t-butylphenyl)-2-methylpropanal, 3-(4-t-butylphenyl)-propanal, 3-(4-isopropylphenyl)-2-methylpropanal, 3-(3,4-methylenedioxyphenyl)-2-methylpropanal, and 2,6-dimethyl-5-heptenal, α-damascone, β-damascone, γ-damascone, β-damascenone, and 6,7-dihydro-1,1,2,3,3-pentamethyl The solid soluble composition according to claim 1, comprising at least one of the following: -4(5H)-indanone, methyl-7,3-dihydro-2H-1,5-benzodioxepin-3-one, 2-[2-(4-methyl-3-cyclohexenyl-1-yl)propyl]cyclopentan-2-one, 2-sec-butylcyclohexanone, and β-dihydroionone, linalool, ethyllinalool, tetrahydrolinalool, dihydromyrcenol, or a mixture thereof.

7. The solid soluble composition according to claim 1, wherein the capsule wall of the fragrance capsule contains at least one of melamine, polyacrylamide, silicone, silica, polystyrene, polyurea, polyurethane, polyacrylate-based materials, polyacrylate esters, gelatin, styrene malic anhydride, polyamide, aromatic alcohol, polyvinyl alcohol, or a mixture thereof.

8. The solid soluble composition according to claim 1, wherein the fragrance capsule has a volume-weighted central capsule diameter of 1 to 100 microns.

9. The solid soluble composition according to claim 1, wherein the freshness beneficial agent is a mixture of the neat fragrance and the fragrance capsule.

10. The solid soluble composition according to claim 1, wherein the fragrance capsule is present in an amount of 0.01% to 15% by weight based on the total weight of the solid soluble composition.

11. The solid soluble composition according to claim 1, wherein the crystallizing agent is present in an amount of 50% to 99% by weight of the solid soluble composition.

12. The solid solubility composition according to claim 1, wherein the stable temperature determined by the thermal stability test method is higher than 40°C.

13. A method for producing a solid soluble composition according to any one of claims 1 to 12, a) To provide at least one of neat fragrance, fragrance capsules, and odor neutralizer, b) Mixing a solid soluble composition mixture by solubilizing the crystallizing agent in water, c) Forming the solid soluble composition mixture by converting and maintaining it to a desired shape and size by at least one of crystallization, partial drying, salt addition, or viscosity increase from liquid crystal formation, d) A method comprising drying by removing water in order to produce a solid soluble composition.

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