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US20190117546A1 - Aerosol Foam Skin Cleanser - Google Patents

Aerosol Foam Skin Cleanser Download PDF

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Publication number
US20190117546A1
US20190117546A1 US16/165,086 US201816165086A US2019117546A1 US 20190117546 A1 US20190117546 A1 US 20190117546A1 US 201816165086 A US201816165086 A US 201816165086A US 2019117546 A1 US2019117546 A1 US 2019117546A1
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Prior art keywords
skin
skin cleanser
cleansing composition
aerosol foaming
packaged aerosol
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Abandoned
Application number
US16/165,086
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English (en)
Inventor
Karl Shiqing Wei
Jean Jianqun Zhao
Somil Manjul SHAH
Wei Ji
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Procter and Gamble Co
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Procter and Gamble Co
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Priority to US16/165,086 priority Critical patent/US20190117546A1/en
Assigned to THE PROCTER & GAMBLE COMPANY reassignment THE PROCTER & GAMBLE COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SHAH, SOMIL MANJUL, WEI, KARL SHIQING, JI, WEI NMN, ZHAO, JEAN JIANQUN
Publication of US20190117546A1 publication Critical patent/US20190117546A1/en
Priority to US17/108,560 priority patent/US11419805B2/en
Abandoned legal-status Critical Current

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/46Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing sulfur
    • A61K8/463Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing sulfur containing sulfuric acid derivatives, e.g. sodium lauryl sulfate
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/02Cosmetics or similar toiletry preparations characterised by special physical form
    • A61K8/04Dispersions; Emulsions
    • A61K8/046Aerosols; Foams
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/31Hydrocarbons
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/33Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing oxygen
    • A61K8/34Alcohols
    • A61K8/342Alcohols having more than seven atoms in an unbroken chain
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/33Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing oxygen
    • A61K8/37Esters of carboxylic acids
    • A61K8/375Esters of carboxylic acids the alcohol moiety containing more than one hydroxy group
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/84Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds obtained by reactions otherwise than those involving only carbon-carbon unsaturated bonds
    • A61K8/87Polyurethanes
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/92Oils, fats or waxes; Derivatives thereof, e.g. hydrogenation products thereof
    • A61K8/922Oils, fats or waxes; Derivatives thereof, e.g. hydrogenation products thereof of vegetable origin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61QSPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q19/00Preparations for care of the skin
    • A61Q19/10Washing or bathing preparations
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/20Chemical, physico-chemical or functional or structural properties of the composition as a whole
    • A61K2800/30Characterized by the absence of a particular group of ingredients
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/80Process related aspects concerning the preparation of the cosmetic composition or the storage or application thereof
    • A61K2800/87Application Devices; Containers; Packaging
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D83/00Containers or packages with special means for dispensing contents
    • B65D83/14Containers for dispensing liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant
    • B65D83/60Containers for dispensing liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant with contents and propellant separated
    • B65D83/62Containers for dispensing liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant with contents and propellant separated by membranes, bags or the like

Definitions

  • a packaged aerosol foaming skin cleanser can include a multiphase skin cleansing composition, a low pressure foaming agent, and a package.
  • Foam cleansers are becoming a popular form among consumers. Foaming cleansers are often micellar with a low viscosity to allow for easy foaming of the product. These thin, micellar compositions, while useful for cleansing, are not the best vehicle for delivery of benefit agents to the skin during the cleansing process. As such, there is a need for an aerosol foam skin cleanser which has the ability to deliver benefit agents to the skin.
  • a packaged aerosol foaming skin cleanser comprising: a) a multiphase skin cleansing composition, comprising a structured surfactant phase and a benefit phase, wherein the structured surfactant phase comprises a branched structured surfactant, and the benefit phase comprises a hydrophobic benefit agent; wherein the multiphase cleansing composition is shear thinning and has a viscosity of about 8,000 cps to about 80,000 cps; b) a low pressure foaming agent; and c) a package.
  • FIG. 1 is a perspective view of an aerosol package
  • FIG. 2A is an exploded view of the aerosol package of FIG. 1 having a bag on valve configuration
  • FIG. 2B is an exploded view of the aerosol package of FIG. 1 having a dip tube configuration.
  • the devices, apparatuses, methods, components, and/or compositions of the present invention can include, consist essentially of, or consist of, the components of the present invention as well as other ingredients described herein.
  • “consisting essentially of” means that the devices, apparatuses, methods, components, and/or compositions may include additional ingredients, but only if the additional ingredients do not materially alter the basic and novel characteristics of the claimed devices, apparatuses, methods, components, and/or compositions.
  • “Foaming agent,” as used herein, refers to a material which is intermingled with a skin cleansing composition inside an aerosol package and results in the skin cleansing composition foaming upon or shortly after exiting an aerosol package.
  • Free of means the stated ingredient has not been added to the aerosol foam skin cleanser, but may incidentally form as a by-product or reaction product of the other components.
  • Low pressure foaming agent refers to a foaming agent with a vapor pressure of about 20 psi or less at a temperature of 21° C. which can be measured using a standard pressure gauge and method on the foaming agent in its canister before addition to an aerosol foam skin cleanser.
  • Low pressure propellant refers to a propellant with a vapor pressure of about 20 psi or less at a temperature of 21° C. which can be measured using a standard pressure gauge and method on the foaming agent in its canister before addition to an aerosol foam skin cleanser.
  • Multiphase when used with respect to skin cleansing compositions, refers to skin cleansing compositions comprising at least two chemically distinct phases (e.g., a structured cleansing phase and a benefit phase). Such phases can be in direct physical contact with one another.
  • the phases of a multiphase skin cleansing composition can be blended or mixed to a significant degree, but still be physically distinct, like a dispersion. In these situations, the physical distinctiveness is often undetectable to the naked eye.
  • the phases are stable and do not significantly phase separate while sitting undisturbed. By no significant phase separation is meant that the composition does not need to be shaken prior to use.
  • the phases are not in the form of an emulsion.
  • the phases may also be in physical contact and visually distinct.
  • the skin cleansing composition can also include a combination blended and visually distinct phases.
  • Non-ionic low HLB Emulsifiers refers to non-ionic surfactants with HLB (hydrophilic and lipophilic balance) values from about 1.5 to about 13.
  • Propellant refers to a material which helps to expel a skin cleansing composition from an aerosol package, but does not interact with the skin cleansing composition until dispensing from the aerosol package.
  • STnS refers to sodium trideceth(n) sulfate, wherein n can define the average number of moles of ethoxylate per molecule.
  • “Structured” as used herein with respect to a composition or a phase means having a rheology that confers stability on the multiphase composition.
  • the degree of structure is determined by characteristics determined by one or more of the following methods: the Young's Modulus Method, Yield Stress Method, or the Zero Shear Viscosity Method, all in the Test Methods section below.
  • a surfactant phase is considered to be structured, if the phase has one or more of the following characteristics: a Yield Stress of greater than about 0.1 Pascal (Pa) to about 300 Pa; a Zero Shear Viscosity of at least about 500 Pascal-seconds (Pa-s) to about 10,000 Pa-s; and/or a Young's Modulus of greater than about 1 Pascal (Pa) to about 300 Pa.
  • compositions While useful for cleansing, are not the best vehicle for delivery of benefit agents to the skin during the cleansing process.
  • structured multiphase compositions are good candidates, like those containing a lamellar phase.
  • Lamellar phase containing compositions are not seen as ideal for foaming.
  • the structure of these compositions usually results in a higher viscosity, above 8,000 cps. Both the structure and the viscosity can make these compositions difficult to foam.
  • the structure helps with the delivery of benefit agents to the skin, it is ideal to maintain the structure of the composition even after addition of a propellant or foaming agent.
  • compositions can be structured in multiple ways.
  • the most common way to structure a composition is through the use of non-surfactant structurants. These materials often consist of larger chain fatty acids or their esters or larger chain fatty alcohols or their ethers. These types of structurants, however, form a more rigid structure which may require high pressure propellant for easy dispensing from the aerosol container.
  • the high pressure propellant causes safety concerns when distributing the aerosol products at high temperature regions. Therefore, there is a need to develop a structured surfactant which can be dispensed with a low pressure foaming agent.
  • One way to overcome the negatives associated with the use of non-surfactant structurants is to utilize structured surfactants, especially in combination with low HLB non-ionic emulsifiers.
  • Structured surfactants with low HLB non-ionic emulsifiers tend to have optimum rheology and compatibility with a low pressure foaming agent.
  • Aerosol products have strict guidelines due to the pressurized nature of the material with the package and the ability of such packages to rupture if the pressure inside the package becomes too high. This can happen, for example, with an increase in external temperature during transport.
  • the high viscosity of structured compositions would lead one to consider the use of higher pressure propellants and/or foaming agents (vapor pressure of about 25 psi or more at 21° C.) for dispensing of the product to overcome the viscosity hurdle of the composition itself.
  • higher pressure propellants and/or foaming agents can be limiting from a distribution standpoint due to the concerns of the package pressure becoming too high during transport and/or storage.
  • High pressure propellants and/or foaming agents Another drawback of the use of high pressure propellants and/or foaming agents is the harshness of such high pressure on the compositions themselves during dispensing.
  • the use of higher pressure propellants and/or foaming agents can place limits on the ingredients which can be used within the formulations.
  • High pressure propellants and/or foaming agents can also work to decrease the density of the product after foaming which can negatively impact the ability of the composition to deposit benefit agents to the skin.
  • the high pressure foaming agent and/or propellant can partition into the benefit phase in the packaged product. Upon dispending the product, the foaming agent and/or propellant quickly evaporates into the gas state and may result in smaller particles of the benefit phase comprising the benefit agents. The smaller particles of the benefit phase comprising the benefit agent could lead to lower deposition of the benefit agent on skin.
  • a high pressure foaming agent creates a low density, low yield stress foam that has the feeling of air upon use and disappears quickly upon lathering.
  • a low pressure foaming agent creates a slow-releasing foam that initially looks like liquid, but when shear is applied, quickly generates denser, higher yield stress, and more stable foam.
  • the preferred rheology for the use of a low pressure foaming agent is as below: a Yield Stress of from about 0.1 Pascal (Pa) to about 300 Pa, from about 0.5 Pa to about 200 Pa, from about 1.0 Pa to about 150 Pa, from about 2.0 Pa to about 100 Pa, from about 5 Pa to about 50 Pa, or from about 10 Pa to about 50 Pa as measured by the Yield Stress Method; a Zero Shear Viscosity of about 500 Pascal-seconds (Pa-s) to about 10,000 Pa-s, about 1,000 Pa-s to about 5,000 Pa-s, or about 1,500 Pa-s to about 5,000 Pa-s; and/or a Young's Modulus of from about 1 Pascal (Pa) to about 300 Pa, from about 5 Pa to about 200 Pa, from about 10 Pa to about 150 Pa, or from about 20 Pa to about 120 Pa.
  • a Yield Stress of from about 0.1 Pascal (Pa) to about 300 Pa, from about 0.5 Pa to about 200 Pa, from about 1.0 Pa to about 150 Pa, from about 2.0 Pa to
  • a skin cleansing composition can be multiphase, for example, the skin cleansing composition may include a cleansing phase and a benefit phase. The cleansing phase and the benefit phase may be in physical contact.
  • a skin cleansing composition may include a combination of multiple phases.
  • a skin cleansing composition may comprise from about 50% to about 99%, by weight of the composition, of a cleansing phase, and from about 1% to about 50%, by weight of the composition, of a benefit phase.
  • the skin cleansing composition may be structured.
  • the skin cleansing composition may also be shear thinning.
  • a cleansing phase can be structured.
  • the structure may include, for example, a lamellar structure or phase.
  • a cleansing phase can include a primary surfactant.
  • the primary surfactant can include a branched anionic surfactant.
  • the primary surfactant can be a structured surfactant.
  • the structured surfactant can include a branched anionic surfactant.
  • a cleansing phase can include, for example, from about 5% to about 30%, or from about 5% to about 25%, by weight of the skin cleansing composition, of a total surfactant.
  • a cleansing phase may include, for example, from about 5% to about 30%, from about 7% to about 25%, or from about 8% to about 22%, by weight of the skin cleansing composition, of a primary surfactant.
  • Structured surfactants can include, for example, sodium trideceth(n) sulfate (STnS).
  • a skin cleansing composition may comprise a co-surfactant.
  • a skin cleansing composition can include from about 1% to about 20%, by weight of the skin cleansing composition, of a co-surfactant.
  • the co-surfactant can include, for example, anionic and zwitterionic surfactants, and non-ionic surfactants.
  • anionic co-surfactants include ammonium lauryl sulfate, ammonium laureth sulfate, triethylamine lauryl sulfate, triethylamine laureth sulfate, triethanolamine lauryl sulfate, triethanolamine laureth sulfate, monoethanolamine lauryl sulfate, monoethanolamine laureth sulfate, diethanolamine lauryl sulfate, diethanolamine laureth sulfate, lauric monoglyceride sodium sulfate, sodium lauryl sulfate, sodium laureth sulfate, potassium laureth sulfate, sodium lauryl sarcosinate, sodium lauroyl sarcosinate, lauryl sarcosine, cocoyl sarcosine, ammonium cocoyl sulfate, sodium cocoyl isethionate, ammonium lauroyl
  • Amphoteric co-surfactants can include those that can be broadly described as derivatives of aliphatic secondary and tertiary amines in which an aliphatic radical can be a straight or branched chain and wherein an aliphatic substituent can contain from about 8 to about 18 carbon atoms such that one carbon atom can contain an anionic water solubilizing group, e.g., carboxy, sulfonate, sulfate, phosphate, or phosphonate.
  • an anionic water solubilizing group e.g., carboxy, sulfonate, sulfate, phosphate, or phosphonate.
  • Zwitterionic co-surfactants suitable for use can include those that are broadly described as derivatives of aliphatic quaternary ammonium, phosphonium, and sulfonium compounds, in which aliphatic radicals can be straight or branched chains, and wherein an aliphatic substituent can contain from about 8 to about 18 carbon atoms such that one carbon atom can contain an anionic group, e.g., carboxy, sulfonate, sulfate, phosphate, or phosphonate.
  • Other zwitterionic surfactants can include betaines, including cocoamidopropyl betaine.
  • a cleansing phase can comprise a nonionic emulsifier.
  • the nonionic emulsifier may be a low HLB emulsifier.
  • a low HLB non-ionic emulsifier has an HLB from about 1.5 to 13.0, from about 3.4 to 13.0, from about 3.4 to about 9.5, or from about 3.4 to about 8.0.
  • the skin cleansing composition can comprise a nonionic emulsifier at concentrations ranging from about 0.1% to about 10%, from about 0.25% to about 8%, from about 0.5% to about 5%, from about 1.0% to about 3%, or from about 1.5% to about 2.5%, by weight of the skin cleansing composition.
  • HLB hydrophile-lipophile balance
  • a cleansing phase may also comprise an associative polymer.
  • the cleansing phase can comprise from about 0.001% to about 5%, from about 0.005% to about 0.5%, from about 0.007% to about 0.05%, from about 0.008% to about 0.04%, or from about 0.01% to about 0.03%, by weight of the personal care composition, of an associative polymer.
  • Such associative polymers can be crosslinked, alkali swellable, associative polymers comprising acidic monomers and associative monomers with hydrophobic end groups, whereby the associative polymer comprises a percentage hydrophobic modification and a hydrophobic side chain comprising alkyl functional groups.
  • the acidic monomers can contribute to an ability of the associative polymer to swell in water upon neutralization of acidic groups; and associative monomers anchor the associative polymer into structured surfactant hydrophobic domains, e.g., lamellae, to confer structure to the surfactant phase and keep the associative polymer from collapsing and losing effectiveness in the presence of an electrolyte.
  • the crosslinked, associative polymer can comprise a percentage hydrophobic modification, which is a mole percentage of monomers expressed as a percentage of a total number of all monomers in a polymer backbone, including both acidic and other non-acidic monomers.
  • Percentage hydrophobic modification of the associative polymer can be determined by the ratio of monomers added during synthesis or by analytical techniques such as proton nuclear magnetic resonance (NMR).
  • Associative alkyl side chains can comprise, for example, butyl, propyl, stearyl, steareth, cetyl, lauryl, laureth, octyl, behenyl, beheneth, steareth, or other linear, branched, saturated, or unsaturated alkyl or alketh hydrocarbon side chains.
  • crosslinked, associative polymers having certain % HM and certain carbon numbers of hydrophobic end groups of alkyl side chains can provide significant enhancement of structure to skin cleansing compositions comprising a structured surfactant, especially to skin cleansing compositions comprising reduced levels of surfactant.
  • Such associative polymers can also provide the above structure at low levels. Concentrations of associative polymers of about 5% or even 10% have been known to provide a sufficient amount structure.
  • the acidic monomer can comprise any acid functional group, for example sulfate, sulfonate, carboxylate, phosphonate, or phosphate or mixtures of acid groups.
  • the acidic monomer can comprise, for example, a carboxylate.
  • the acidic monomer can be an acrylate, including acrylic acid and/or methacrylic acid.
  • the acidic monomer can comprise a polymerizable structure, e.g., vinyl functionality. Mixtures of acidic monomers, for example acrylic acid and methacrylic acid monomer mixtures, may be useful as well.
  • An exemplary associative polymer can include AQUPEC® SER-300 made by Sumitomo Seika of Japan, which is an acrylate/C 10 -C 30 alkyl acrylate cross-polymer and comprises stearyl side chains with less than about 1% HM.
  • Associative polymers can comprise about C 16 (cetyl) alkyl hydrophobic side chains with about 0.7% hydrophobic modification, but a percentage hydrophobic modification can be up to an aqueous solubility limit in surfactant containing compositions (e.g., up to 2%, 5%, or 10%).
  • non-associative polymers can include biopolymer polysaccharides (e.g., xanthan gum, gellan gum), cellulosic polysaccharides (e.g., carboxymethyl cellulose, carboxymethyl hydroxyethyl cellulose), other polysaccharides (e.g., guar gum, hydroxypropyl guar, and sodium alginate), synthetic hydrocarbon polymers (e.g., polyacrylamide and copolymers, polyethylene oxide, polyacrylic acid copolymers), and combinations thereof.
  • biopolymer polysaccharides e.g., xanthan gum, gellan gum
  • cellulosic polysaccharides e.g., carboxymethyl cellulose, carboxymethyl hydroxyethyl cellulose
  • other polysaccharides e.g., guar gum, hydroxypropyl guar, and sodium alginate
  • synthetic hydrocarbon polymers e.g., polyacrylamide and copolymers,
  • a skin cleansing composition can also comprise a cationic deposition polymer.
  • the cationic deposition polymer can be present in an amount of 0.1% to about 2%, by weight of the skin cleansing composition.
  • Suitable cationic deposition polymers can contain cationic nitrogen-containing moieties such as quaternary moieties.
  • Non-limiting examples of cationic deposition polymers can include polysaccharide polymers, such as cationic cellulose derivatives.
  • Cationic cellulose polymers can be salts of hydroxyethyl cellulose reacted with trimethyl ammonium substituted epoxide, referred to in the industry (CTFA) as Polyquaternium 10, which can be available from Amerchol Corp.
  • CTFA trimethyl ammonium substituted epoxide
  • a cleansing phase may also include an electrolyte.
  • Electrolytes may be present at a level of about 1% to about 10%, by weight of the skin cleansing composition.
  • Suitable electrolytes can include anions such as phosphate, chloride, sulfate, citrate, and mixtures thereof and cations such as sodium, ammonium, potassium, magnesium, and mixtures thereof.
  • suitable electrolytes can include sodium chloride, ammonium chloride, sodium sulfate, ammonium sulfate, and mixtures thereof.
  • a cleansing phase may include water.
  • the cleansing phase can comprise from about 10% to about 90%, from about 40% to about 85%, or from about 60% to about 80%, by weight of the skin cleansing composition, of water.
  • a benefit phase can comprise a hydrophobic benefit agent.
  • a skin cleansing composition may include from about 0.1% to about 20%, by weight of the skin cleansing composition, of a hydrophobic benefit agent.
  • a hydrophobic benefit agent can be insoluble in the cleansing phase.
  • Suitable benefit agents can include, for example, petrolatum, monoglyceryl monooleate, mineral oil, glycerides (e.g., soybean oil), sucrose polyesters, lanolin, lanolin derivatives, lanolin esters, lanolin oil, natural waxes, synthetic waxes, volatile organosiloxanes, derivatives of volatile organosiloxanes, non-volatile organosiloxanes, derivatives of non-volatile organosiloxanes, natural triglycerides, synthetic triglycerides, and mixtures thereof.
  • SEFOSE® includes one or more types of sucrose polyesters.
  • Sucrose polyesters are derived from a natural resource and therefore, the use of sucrose polyesters as the benefit agent can result in a positive environmental impact.
  • Sucrose polyesters are polyester materials having multiple substitution positions around the sucrose backbone coupled with the chain length, saturation, and derivation variables of the fatty chains.
  • Such sucrose polyesters can have an esterification (“IBAR”) of greater than about 5.
  • the sucrose polyester may have an IBAR of about 5 to about 8.
  • the sucrose polyester may have an IBAR of about 5-7; in another example, the sucrose polyester can have an IBAR of about 6.
  • the sucrose polyester can have an IBAR of about 8.
  • sucrose polyesters suitable for use include SEFOSE® 1618S, SEFOSE® 1618U, SEFOSE® 1618H, Sefa Soyate IMF 40, Sefa Soyate LP426, SEFOSE® 2275, SEFOSE® C1695, SEFOSE® C18:0 95, SEFOSE® C1495, SEFOSE® 1618H B6, SEFOSE® 1618S B6, SEFOSE® 1618U B6, Sefa Cottonate, SEFOSE® C1295, Sefa C895, Sefa C1095, SEFOSE® 1618S B4.5, all available from The Procter and Gamble Co. of Cincinnati, Ohio. Sucrose polyesters can also be combined with other benefit agents in the benefit phase.
  • Other examples can include hexyl laurate, isohexyl laurate, myristyl myristate, isohexyl palmitate, decyl oleate, isodecyl oleate, hexadecyl stearate, decyl stearate, isopropyl isostearate, diisopropyl adipate, diisohexyl adipate, dihexyldecyl adipate, diisopropyl sebacate, acyl isononanoate lauryl lactate, myristyl lactate, cetyl lactate, and combinations thereof.
  • Non-limiting examples of alkenyl esters suitable for use as hydrophobic benefit agents herein can include oleyl myristate, oleyl stearate, oleyl oleate, and combinations thereof.
  • Non-limiting examples of polyglycerin fatty acid esters suitable for use as hydrophobic benefit agents herein can include decaglyceryl distearate, decaglyceryl diisostearate, decaglyceryl monomyriate, decaglyceryl monolaurate, hexaglyceryl monooleate, and combinations thereof.
  • Non-limiting examples of silicone oils suitable for use as hydrophobic benefit agents herein can include dimethicone copolyol, dimethylpolysiloxane, diethylpolysiloxane, mixed C 1 -C 30 alkyl polysiloxanes, phenyl dimethicone, dimethiconol, and combinations thereof.
  • Still other suitable hydrophobic skin benefit agents can include milk triglycerides (e.g., hydroxylated milk glyceride) and polyol fatty acid polyesters.
  • a skin cleansing may also include additional materials in any phase.
  • these materials can include for example, perfume, colorants, antimicrobials, pH modifiers, and the like. Such materials are usually formulated at about 6% or less, about 5% or less, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.5% or less, about 0.25% or less, about 0.1% or less, about 0.01% or less, or about 0.005% or less by weight of the personal care composition.
  • Suitable hydrocarbon foaming agents can include those which have a vapor pressure of about 20 psi or less at 21° C.
  • this could include n-butane, an isobutane blend, isopentane, compressed gases such as carbon dioxide, nitrous oxide, nitrogen, compressed air, or a combination thereof.
  • n-butane has a vapor pressure of about 17 psi when measured at 21° C.
  • An isobutene blend can include, for example, a combination of isobutane and isopentane with about 25 weight percent of the isobutane and about 75 weight percent of the isopentane, by weight of the blend. This blend has a vapor pressure of about 7 psi at a temperature of 21° C.
  • the low pressure foaming agent for use in the aerosol foam skin cleanser can also be selected from the group consisting of halogenated alkenes of generic formula that would include numerous HFOs and HCFOs.
  • the foaming agent listed can be mixed with one or more hydrofluoroolefins (HFOs), hydrochlorofluoroolefins (HCFOs), hydrofluorocarbons (FFCs), chlorofluorocarbons (CFCs), hydrocarbons, alkyl ethers, and compressed gases.
  • the low pressure foaming agent can comprise trans-1-chloro-3,3,3-trifluoropropene (Solstice® HCFO-1233zd), from Honeywell with a vapor pressure of about 16.3 psi at 21° C.
  • the aerosol foam skin cleanser may also comprise a low pressure propellant.
  • a low pressure propellant may include any of those described above as a low pressure foaming agent.
  • a low pressure propellant may be present at a level of about 1% to about 20%, by weight of the aerosol foam skin cleanser.
  • propellant is injected into the canister package during the crimping process as the driving force to compress a bag that is attached to the valve.
  • This process is called “pressure crimping”.
  • Pressure crimping can be accomplished using the technology of under-the-cup gassing.
  • the target is a pressure.
  • the target pressure would be 20 psi or less at a temperature of 21° C.
  • the package could be filled with a propellant to a pressure of about 11 to about 15 psi.
  • the aerosol foam skin cleanser may be included in any suitable type of aerosol package 20, see FIG. 1 .
  • An aerosol package can include a container body 22 and a cap 30.
  • An aerosol package can be, for example, in a dip tube configuration (see FIG. 2B ) or a bag in bottle configuration, like the bag on valve configuration (see FIG. 2A ).
  • the aerosol package 20 may have a cap 30, a valve assembly 28 attached to at least a portion of the cap 30, a valve cup 26 which may be attached to the neck 24 of the container body 22 and to the valve assembly 28.
  • a collapsible bag 32 may be attached to the valve cup 26 and contain an aerosol foam skin cleanser 42.
  • a propellant 40 may be contained between the collapsible bag 32 and the exterior wall 25 of the container body 22.
  • a dip tube 34 can be attached to a valve cup 26 and reside inside the container body 22 in contact with an aerosol foam skin cleanser 42.
  • the viscosity of a skin cleansing composition can be assessed by the T-Bar Viscosity Method.
  • the apparatus for T-Bar measurements includes a Brookfield DV-II+ Pro Viscometer with Helipath Accessory; a chuck, weight and closer assembly for T-bar attachment; a T-bar Spindle D, a personal computer with Rheocalc software from Brookfield, and a cable connecting a Brookfield Viscometer to a computer.
  • the T-Bar viscosity is an average T-Bar viscosity reading between the 10th reading and the 90th reading (the first ten readings and the last ten readings are not used for the average T-Bar viscosity calculation).
  • the T-Bar viscosity reading is provided in cP.
  • the Zero Shear Viscosity of a material which is a phase or a component of the skin cleansing composition can be measured either prior to combining in the skin cleansing composition, after preparing a composition, or first separating a phase or component from a personal care composition by suitable physical separation means, such as centrifugation, pipetting, cutting away mechanically, rinsing, filtering, or other separation means.
  • suitable physical separation means such as centrifugation, pipetting, cutting away mechanically, rinsing, filtering, or other separation means.
  • the timing of the measurement can depend on what is available. For example, if a final product is all that is available and a phase of the product is the target for measurement, then the phase will be separated prior to measurement.
  • a controlled stress rheometer such as a TA Instruments AR2000 Rheometer is used to determine the Yield Stress and Zero Shear Viscosity. The determination is performed at 25° C. with a 4 cm diameter parallel plate measuring system and a 1 mm gap. The geometry has a shear stress factor of 79580 m-3 to convert torque obtained to stress. Serrated plates can be used to obtain consistent results when slip occurs.
  • the target material is positioned on a rheometer base plate; the measurement geometry (upper plate) is moved into position 1.1 mm above the base plate. Excess material at the geometry edge is removed by scraping after locking the geometry. The geometry is then moved to the target 1 mm position above the base plate and a pause of about 2 minutes is allowed to allow loading stresses to relax. This loading procedure ensures no tangential stresses are loaded at the measurement onset which can influence the results obtained. If the material comprises particles discernible to the eye or by feel (e.g., beads) that are larger than about 150 microns in number average diameter, the gap setting between the base plate and upper plate is increased to the smaller of 4 mm or 8-fold the diameter of the 95th volume percentile particle diameter. If a phase has any particle larger than 5 mm in any dimension, the particles are removed prior to the measurement.
  • the material comprises particles discernible to the eye or by feel (e.g., beads) that are larger than about 150 microns in number average diameter
  • the gap setting between the base plate and upper plate
  • the measurement is performed by applying a continuous shear stress ramp from 0.1 Pa to 1,000 Pa over a time interval of 4 minutes using a logarithmic progression, i.e., measurement points evenly spaced on a logarithmic scale. Thirty measurement points per decade of stress increase are obtained. Stress, strain, and viscosity are recorded. If the measurement result is incomplete, for example, if material is observed to flow from the gap, results obtained are evaluated with incomplete data points excluded. If there are insufficient points to obtain an accurate measurement, the measurement is repeated with increased number of sample points.
  • the Yield Stress is determined as follows. Stress (Pa) and strain (unitless) data are transformed by taking their logarithms (base 10). Log(stress) is graphed vs. log(strain) for only the data obtained between a stress of 0.2 Pa and 2.0 Pa, about 30 points. If the viscosity at a stress of 1 Pa is less than 500 Pa-sec but greater than 75 Pa-sec, then log(stress) is graphed vs. log(strain) for only the data between 0.2 Pa and 1.0 Pa, and the following mathematical procedure is followed.
  • the zero shear viscosity is the median of the 4 highest viscosity values (i.e., individual points) obtained in the test, the yield stress is zero, and the following mathematical procedure is not used.
  • a predicted value of log(strain) is obtained using the coefficients m and b obtained, and the actual stress, using Equation (1).
  • a predicted strain at each stress is obtained by taking the antilog (i.e., 10.sup.x for each x). The predicted strain is compared to the actual strain at each measurement point to obtain a % variation at each point, using Equation (2).
  • the Yield Stress is the first stress (Pa) at which % variation exceeds 10% and subsequent (higher) stresses result in even greater variation than 10% due to the onset of flow or deformation of the structure.
  • the Young's Modulus (Pa) is obtained by graphing Stress (Pa) vs. Strain (unitless) and obtaining a slope of a regression line of an initial linear region between Stress vs. Strain, typically occurring in the region below about 4% strain. If the relationship is not linear, the linear regression line slope below 2% strain is taken as the Young's Modulus (Pa), using unitless strain.
  • the Zero Shear Viscosity is obtained by taking a first median value of viscosity in Pascal-seconds (Pa-s) for viscosity data obtained between and including 0.1 Pa and a point where viscosity begins to steeply decline. After taking the first median viscosity, all viscosity values greater than 5-fold the first median value and less than 0.2 ⁇ the median value are excluded, and a second median viscosity value is obtained of the same viscosity data, excluding the indicated data points. The second median viscosity so obtained is the Zero Shear Viscosity.
  • Pa-s Pascal-seconds
  • a phase or composition can be considered to be structured if it has a Zero Shear Viscosity of about 500 Pascal-seconds (Pa-s) to about 10,000 Pa-s, a Yield Stress of greater than about 0.1 Pascal (Pa) to about 300 Pa, and/or a Young's Modulus of greater than about 1 Pascal (Pa) to about 300 Pa.
  • the amount of deposition of a benefit agent can be measured in vitro.
  • the In-Vitro deposition method measures the deposition of benefit agents on a mechanically stressed skin mimic. The method compares spectral data of the skin mimic surface material before and after cleansing in an automated cleansing unit.
  • the In-Vitro deposition method uses two 96-well microplates (hereinafter referred to as “microplates”). Suitable 96-well microplates are commercially available from PerkinElmer and from VWR.com.
  • the SpectraPlate 96-MG from PerkinElmer has 8 rows and 12 columns with a well volume of 400 .mu.l.
  • the SpectraPlate 96-MG comprises the approximate dimensions of 14.6 mm in height, 127.8 mm in length and 85.5 mm in width.
  • the SpectraPlate 96-MG has a well diameter of 7.15 mm, a well depth of 10.8 and a well to well spacing of 9.0 mm
  • a 96-well microplate is provided for containing the samples to be measured.
  • the in-vitro deposition method uses approximately 1536 bodies. Each body is approximately 2 mm in circumference spherical stainless steel bearings that comprise ferrometallic material, such as those available from WLB Antriebes institute Gmbh, Scarrastrasse 12, D-68307 Mannheim, Germany Eight bodies carefully loaded into each of the 96 wells of microplates to ensure the same number is loaded into each well.
  • the skin cleansing compositions are prepared according to the description in the Example Section below.
  • samples are prepared by combining a personal care composition and distilled water.
  • 90+ ⁇ 0.02 grams of distilled water is dispensed into a mixing vessel.
  • the mixing vessel is secured to the base of a mixer, such as a table top mixer from IKA, the mixer blades are adjusted into the distilled water within the mixing vessel.
  • a syringe is then zeroed on a balance.
  • the syringe is filled with the designated skin cleansing composition.
  • the syringe is weighed and small amounts of the designated skin cleansing composition are dispensed until 10 grams of the skin cleansing composition remains in the syringe.
  • the mixer is turned on at a speed of 500 rpm and the contents of the syringe are dispensed into distilled water within the mixing vessel.
  • the distilled water and the designated skin cleansing composition are mixed for 2 minutes at 500 rpm forming the sample.
  • the sample is withdrawn by syringe from the mixing vessel while the mixer is on at a speed of 300 rpm.
  • the mixing and dispensing procedures are followed for mixing and dispensing for the control sample and the test samples 1-5. After the samples are prepared, the control samples and test samples are dispensed in the specified wells of the microplate.
  • the skin mimic used in the in-vitro deposition methods is comprised of a molded bicomponent polyethylene substrate.
  • the skin mimic is textured on one side with a pattern that resembles the texture of human skin.
  • the textured side of the skin mimic is coated with 1,1,1-trimethyl-1-pentene that is plasma deposited.
  • the skin mimic has a total surface energy of 32+/ ⁇ 1.0 (mJ/m 2 ), a zeta potential of ( ⁇ ) 27.4 (mV), a contact angle in water of 100° F.+/ ⁇ 2.0.
  • a pattern resembling the texture of human forearm skin is formed from a photograph image of human forearm skin. The pattern is transferred to a clear sheet to form a mask. A DuPont®MX series dry film photoresists is adhered to the metal sheet. The mask is placed on top of the metal sheet to form a metal/photoresist/mask. The composite of metal/photoresist/mask is exposed to an appropriate dose of UV light, using industry standard exposure tools.
  • the substrate is placed on a perforated aluminum sample tray in between parallel plate aluminum electrodes in the vacuum chamber and the vacuum chamber pressure is reduced to approximately 100 milliTorr (mTorr).
  • the substrate to be plasma coated is substantially degassed by adding a mixture of argon and nitrogen gas into the vacuum chamber at flow rates of 20 sccm of argon and 10 sccm of nitrogen, (where “sccm” means standard cubic centimeter per minute) for about one hour.
  • the vacuum chamber pressure is reduced to 10 mTorr and 25 W of continuous wave RF power is applied for approximately 5 minutes while allowing the argon/nitrogen gas mixture to flow into the vacuum chamber at flow rates of 20 sccm of argon and 10 sccm of nitrogen.
  • the release of gas is stopped and vacuum chamber is evacuated to the pressure of 10 mTorr.
  • the 1,1,1-trimethyl-1-pentene coating material available from Aldrich is introduced into the vacuum chamber to a pressure of 100 mTorr at a flow rate selected is from about 10 sccm to 200 sccm depending the knowledge of or may be determined with limited experimentation by one of ordinary skill in the art.
  • the coating material is introduced into the vacuum chamber 25 W of continuous wave RF power is applied for approximately 25 minutes while maintaining a vapor pressure of approximately 100-120 mTorr.
  • the plasma deposition results in a polymeric coating of 1,1,1-trimethyl-1-pentene that is covalently bonded to the substrate. The exact times for plasma deposition will be within the knowledge or may be determined with limited experimentation by one of skill in the art.
  • the power to the plasma unit is turned off and the flow of the coating material is stopped.
  • the vacuum chamber is purged with about 20 sccm argon for about 30 min prior to the removal of the coated substrate.
  • the pieces of skin mimics are arranged over the openings of the wells of the microplates.
  • the pieces of skin mimic surface material are transferred to cover the openings of the wells of the each of the microplates to ensure that the textured and treated region of the skin mimic is facing the openings of the wells of the microplate.
  • a lid is placed over each piece of the skin mimic and the associated microplate to form a lidded microplate.
  • Suitable rodless air slides comprise a one inch bore and eleven inch stroke and have associated end lugs and mount brackets, which are commercially available from McMaster-Carr.
  • the rodless air slide is double acting and comprises a carriage that is connected to an internal piston and two compressed air ports.
  • the automated cleansing unit comprises two magnetic arms.
  • the horizontal support comprising a rodless air slide is the structure upon which the two magnetic arms are mounted.
  • the magnetic arms are mounted to the rodless air slide such that the magnetic arms move back and forth along the length of the double acting rodless air slide by the force of compressed air.
  • Each of the magnetic arms are comprised of aluminum and have the approximate dimensions of one inch by two inches by fourteen inches in length and have a “T” shape channel that houses seven neodymium iron boron magnets (not shown).
  • Each of the neodymium iron boron magnets has the approximate dimensions of two inches in length, one inch in width and half or an inch in height.
  • Each of the microplate holders comprise a clamping plate and four pistons attached to a pneumatic control unit.
  • the pistons for the pneumatic control unit hold the microplates in the four microplate holders at a pressure of from about 90 psi.
  • the pneumatic control unit Prior to placing the lidded microplates into the microplate holders of automated cleansing unit, the pneumatic control unit is turned on.
  • the pneumatic control unit is used to apply compressed air to the automated cleansing unit, which imparts a force by converting the potential energy of compressed air into kinetic energy.
  • the pneumatic control unit comprises a solenoid air control valve, a distribution manifold outlet, a compressed air control valve, a compressed air flow regulator, an alternating output binary valve, a two-hand safety pneumatic control valve, a compressed air control valve and various connectors that provide pressurized air to the automated cleansing unit from an external air source.
  • the air control valve, air flow regulators, alternating a binary valves, a two-hand safety pneumatic control valve are positioned upstream of a solenoid air control valve.
  • a suitable solenoid air control valve in one embodiment, is described as a double air style valve with a 10 psi to 120 operating pressure.
  • Suitable compressed air flow regulators can operate in the pressure range of 14 psi to 116 psi.
  • Suitable air control valve alternating output binary valves operate in a 35 psi to 100 psi range. All of the components of the pneumatic control unit are available from McMaster-Carr®.
  • the microplate holder is designed to hold four commercially available 96 well microplates.
  • the microplate holder comprises a riser, an aluminum base plate, a clamping plate and pistons.
  • Riser has a larger dimension than the approximately dimension of a commercially available microplate. In some embodiments, the riser has the dimensions five inches by five and 3 ⁇ 4 inches.
  • the riser is comprised of polyoxymethylene which is commonly known under DuPont's brand name DELRIN®® is used as a metal substitute because it is a lightweight, low-friction, and wear-resistant thermoplastic that possesses good physical and processing properties and capable of operating in temperatures in excess of 90° C.
  • the microplate holder in some embodiments, comprises an aluminum base plate.
  • the aluminum base plate has a raised portion and a trench which is approximately the same dimensions as a commercially available microplate, such that the bottom of the wells rest on the raised portion and the perimeter of the microplate fit in the trench.
  • the aluminum base plate is designed such that the microplate is not adversely affected by the compression of the clamping plate by the piston when the pneumatic pressure unit is actuated.
  • the aluminum base plate comprises a first heater and the clamping plate comprises a second heater.
  • the first heater and second heater comprise flexible silicone rubber heaters available from Omega.com.
  • the first heater and the second heater can be controlled by a 1 ⁇ 4 DIN six zone temperature controller with RS-232 communications and free configuration software available by from Omega.com.
  • the first heater and the second heater are used to stabilize the temperature of the sample and the skin mimic at room temperature ranging from about 20° C. to about 25° C.
  • the first heater and the second heater Prior to placing the lidded microplates into the microplate holders of automated cleansing unit, the first heater and the second heater are turned on to stabilize the temperature of the sample and the skin mimic at room temperature ranging from about 20° C. to about 25° C.
  • the lidded microplates are placed into the microplate holders and pneumatic control unit is actuated such that the lidded microplates are held under 90 psi of pressure.
  • the magnetic arms are actuated on and arms moves over the lidded microplates at a height of 2.65 cm above the microplate holders.
  • the magnetic arms of the automated cleansing unit sweep back and forth over the microplate holders for 5 minutes, at a speed of 6 sweeps per every 10 seconds.
  • the lidded microplates are removed from the microplate holders and are disassembled so that spectral data is gathered by a spectrophotometer for both pieces of skin mimic surface material.
  • the first piece of skin mimic is placed on the reading surface with the textured and treated region of the first skin mimic facing the spectrophotometer.
  • a piece of plastic having a plurality of holes which correspond in size to the openings of the microplate is placed over the textured and treated region of the first skin mimic.
  • the scan is then performed using the robot arm of the spectrophotometer.
  • the baseline spectral data for the first piece of skin mimic material is saved for comparison with the first baseline.
  • the reading surface of the spectrophotometer is cleaned and the spectral data for the second piece of skin mimic surface material is obtained by the aforesaid method.
  • the baseline spectral data for the second skin mimic surface material is saved on a computer for comparison with the second baseline.
  • the spectrophotometer measures the L-a-b values for the skin mimic surface material before cleansing and after washing.
  • the deposition values of the in-vitro method are reported as a Delta L value and are indicative of the deposition profile of each sample.
  • the difference of the light intensity L or “Delta-L” is the L value after the cleansing-L value before cleansing (the baseline spectral data).
  • the Deposition Method is also available in U.S. Patent Application Pub. No. 20100158830.
  • Inventive Example 1 is a skin cleansing composition which can be included as part of an aerosol foam skin cleanser.
  • Inventive Example 1 is a blended multiphase composition, wherein the benefit phase (including petrolatum, soybean oil, butylated hydroxyltoluene, and monoglyceryl monooleate) is dispersed in a cleansing phase.
  • This composition is made by adding water to a main mixing vessel.
  • Sodium chloride, xanthan gum, guar hydroxypropyltrimonium chloride, and sodium trideceth sulfate are added to the water with constant mixing. While that is mixing, a polymer premix is prepared by combining Acrylates/C10-30 Alkyl Acrylates and PEG-90M into trideceth-3 with mixing. Once the polymer premix is dispersed, the premix is added to the main mixing vessel.
  • Cocamidopropyl betaine, EDTA, and sodium benzoate are then sequentially added to the main mixing vessel with mixing.
  • the pH is then adjusted to about 5.7 with the addition of a pH modifier (like citric acid).
  • Preservative and perfume are then added with mixing.
  • the benefit phase is prepared by first creating a lipid premix by heating soybean oil to about 50° C. in a separate vessel. Monoglyceryl monooleate and butylated hydroxyltoluene are added to the soybean oil with mixing. The lipid premix is then added to the main vessel with stirring. In a separate vessel, petrolatum is heated to about 88° C. with mixing. The petrolatum is then cooled to about 60° C. and added to the main mixing vessel with mixing. The composition is mixed until homogenous.
  • Inventive Examples 2-7 are of aerosol foam skin cleansers including a skin cleansing composition (Inventive Example 1), a low pressure foaming agent, and a package.
  • Inventive Examples 2-7 are made by first premixing the skin cleansing composition with foaming agent in a closed system and then injecting the mixture into a bag which is fastened to a valve through the standard crimping process. Then, the valve with bag and mixture is crimped onto a can (either metal, plastic, or glass). Then, propellant is added into the can, but outside of the bag to provide a positive pressure differential outside of the bag.
  • Inventive Example 8 is a skin cleansing composition which can be included as part of an aerosol foam skin cleanser.
  • Inventive Example 8 is a blended multiphase composition, wherein the benefit phase (including soybean oil, butylated hydroxyltoluene, and monoglyceryl monooleate) is dispersed in the cleansing phase.
  • This composition is made by adding water to a main mixing vessel. Sodium chloride, guar hydroxypropyltrimonium chloride, sodium trideceth sulfate, and cocamidopropyl betaine are added to the water with constant mixing. Then add EDTA and sodium benzoate. The pH is then adjusted to about 5.7 with the addition of a pH modifier (like citric acid). Then add the preservative and perfume with good mixing.
  • a pH modifier like citric acid
  • the benefit phase is prepared by first creating a lipid premix by heating soybean oil to about 50° C. in a separate vessel. Monoglyceryl monooleate and butylated hydroxyltoluene are added to the soybean oil with mixing. The lipid premix is then added to the main vessel with stirring. The composition is mixed until homogenous.
  • Inventive Example 9 is an aerosol foam skin cleanser including a skin cleansing composition (Inventive Example 8), a low pressure foaming agent, and a package.
  • Example 9 Skin Cleansing Composition (Example 8) 97.15% Foaming agent (about 25 wt % isobutane & about 75 wt 2.85% % isopentane) Packaging Bag on Valve Propellant - Compressed Air filled to a pressure of about Yes 12-15 psi Foam Density (g/ml) 0.85
  • Inventive Example 9 is made by first premixing the structured surfactant composition with foaming agent in a closed system and then injecting the mixture into a bag which is fastened to a valve through the standard crimping process. Then, the valve with bag and mixture is crimped onto a can (either metal, plastic, or glass). Then, propellant is added into the can, but outside of the bag to provide a positive pressure differential outside of the bag.
  • Inventive Example 10 is a skin cleansing composition which can be included as part of an aerosol foam skin cleanser.
  • Inventive Example 10 is a blended multiphase composition, wherein the benefit phase (including soybean oil, butylated hydroxytoluene, and monoglyceryl monooleate) is dispersed in a cleansing phase.
  • This composition is made by adding water to a main mixing vessel.
  • Sodium chloride, xanthan gum, guar hydroxypropyltrimonium chloride, and sodium trideceth sulfate are added to the water with constant mixing. While that is mixing, a polymer premix is prepared by combining Acrylates/C10-30 Alkyl Acrylates into trideceth-3 with mixing. Once the polymer premix is dispersed, the premix is added to the main mixing vessel.
  • Cocamidopropyl betaine, EDTA, and sodium benzoate are then sequentially added to the main mixing vessel with mixing.
  • the pH is then adjusted to about 5.7 with the addition of a pH modifier (like citric acid).
  • the preservative and perfume are then added with good mixing.
  • Inventive Example 11 is an aerosol foam skin cleanser including a skin cleansing composition (Inventive Example 10), a low pressure foaming agent, and a package.
  • Example 11 Skin Cleansing Composition (Example 10) 95% Foaming agent (n-butane) 5% Packaging Dip Tube
  • Inventive Example 11 is made by first premixing the skin cleansing composition with foaming agent in a closed system and then injecting the mixture into a canister.

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US10987290B2 (en) 2017-10-20 2021-04-27 The Procter And Gamble Company Aerosol foam skin cleanser
US11207261B2 (en) 2014-11-10 2021-12-28 The Procter And Gamble Company Personal care compositions with two benefit phases
US11207248B2 (en) 2014-11-10 2021-12-28 The Procter And Gamble Company Personal care compositions with two benefit phases
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US11365397B2 (en) 2018-11-29 2022-06-21 The Procter & Gamble Company Methods for screening personal care products
US11419805B2 (en) 2017-10-20 2022-08-23 The Procter & Gamble Company Aerosol foam skin cleanser

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US11419805B2 (en) 2022-08-23
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EP3697374B1 (fr) 2022-02-16
US20210077372A1 (en) 2021-03-18

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