WO2024214063A1 - Method for preservation of an active compound, formulation and preservative - Google Patents
Method for preservation of an active compound, formulation and preservative Download PDFInfo
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- WO2024214063A1 WO2024214063A1 PCT/IB2024/053608 IB2024053608W WO2024214063A1 WO 2024214063 A1 WO2024214063 A1 WO 2024214063A1 IB 2024053608 W IB2024053608 W IB 2024053608W WO 2024214063 A1 WO2024214063 A1 WO 2024214063A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/06—Making microcapsules or microballoons by phase separation
- B01J13/14—Polymerisation; cross-linking
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/30—Encapsulation of particles, e.g. foodstuff additives
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
- A61K8/11—Encapsulated compositions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/73—Polysaccharides
- A61K8/733—Alginic acid; Salts thereof
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
- B01J13/046—Making microcapsules or microballoons by physical processes, e.g. drying, spraying combined with gelification or coagulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/20—After-treatment of capsule walls, e.g. hardening
- B01J13/203—Exchange of core-forming material by diffusion through the capsule wall
Definitions
- the present invention relates to a method for preservation of an active compound, as well to a preservative and a formulation.
- the present invention provides a method for preservation of an active compound, wherein a powder of said active compound is provided, wherein said powder is dispersed in an at least partly gellable or crystallizable liquid hydrophobic material to form a suspension or dispersion containing said powder, wherein said suspension or dispersion is formed into micro-bodies, wherein said micro-bodies are encapsulated by a polymer shell to form suspension- or dispersion-laden micro-bodies which contain one or multiple cores of said suspension or dispersion, wherein said suspension- or dispersion-laden micro-bodies are solidified, particularly gelled and/or crystallized, to form micro-bodies containing said active compound in an at least substantially solidified hydrophobic network.
- micro-bodies can also be referred to interchangeably as “microdroplets”, “micro-capsules” or “micro-particles”, while the adjective “micro” refers to sizes ranging from a sub-micron, particularly nano, scale to several millimetres.
- the descriptor "(partly or completely) solidified, particularly gelled and/or crystallized, hydrophobic network” can also be referred to as “oleogel” and vice versa.
- Oleogels sometimes also called organo-gels, are gels having a continuous phase of oil. Oleogel networks are characterized by their capacity to retain substantial amounts of oil. Oleogels are further characterized by their thermo-reversible, viscoelastic, and (under certain conditions) substantially self-standing properties.
- the oleogel may be applied in combination with a hydrogel, also referred to as a bi-gel.
- micro-bodies can have a diameter or maximum dimension ranging from several micrometre (or micron), particularly several tens of micrometre, particularly a few hundred micrometre, up to a few millimetre. Due to the relative small dimension of the micro-bodies, the active compound may still readily be used as a powdery or granular ingredient in a variety of applications, formulations, and products. The powder comprising the active compound is captured inside these water-free micro-bodies that protect the compound against the external environment.
- a preservative for an active compound comprises one or more preserving micro-bodies, each having at least one core surrounded by a shell that is formed by a polymer network, wherein said core comprises an at least substantially solidified, particularly gelled, gellable or crystallizable liquid hydrophobic material, particularly an oleogel, and a solid powder, said powder being dispersed throughout said core, and wherein said powder comprises said active compound.
- the invention provides for a formulation comprising an active compound in a preserved state by means of such preservative.
- a formulation comprising an active compound in a preserved state by means of such preservative.
- Such formulation may be applied in or as a cosmetic product, a personal care or home care product, a dermatological product, a food or nutrition product, an agrochemical product, a fragrance product, a health or healthy product, a pharmaceutical product, a (bio)medical product, a household product, an energy storage product, a coatings product, or an adhesives product.
- the active compound is dispersed and captured inside a substantially water-free, hydrophobic and air-tight environment provided by the oleogel surroundings of said core.
- the core also appears to substantially prevent both the release and dissolution of the powder into aqueous and/or hydrophilic solvents, formulations or surroundings with which the micro-bodies may be mixed.
- the polymer shell holds the core together and avoids deformation, merging, or damaging of the oleogel cores and individual micro-bodies.
- the polymer shell enables facile handling such as drying, mixing and/or blending of the hydrophobic oleogel into other formulations such as cosmetic, food, and pharmaceutical formulations, including non-oil-based and hydrophilic, for example, water-based formulations.
- the polymer shell may be designed to disintegrate or break under induced chemical or mechanical conditions, upon which said active compound comprising powder is released from the micro-body.
- the active compound is, as it was, entrapped and substantially hermetically canned inside a micro-body until being released.
- the active compound can be released via mechanical and chemical conditions or triggers.
- Such induced conditions or triggers may for instance include shear stress, like for instance rubbing on the skin or brushing, for example by means of a paint brush, compression, like chewing, a combination of shear and compression, for instance extrusion or injection through a small dispenser like a needle or spray nozzle, disintegration of the core or the shell, for instance by chelation, freeze-thaw cycles, or heating, particularly to promote oleogel melting, hydrolyzation, photodegradation, diffusion, burning, acidic or enzymatic degradation or fermentation, for instance in the stomach, ileum, colon, or any other part of the gastrointestinal tract, or any other form of mechanical and/or chemical stress that results in the escape of the active compound from a micro-body.
- shear stress like for instance rubbing on the skin or brushing
- compression like chewing
- a combination of shear and compression for instance extrusion or injection through a small dispenser like a needle or spray nozzle
- disintegration of the core or the shell for instance by chelation,
- the micro-bodies may be exposed to a solution comprising citric acid, where said citric acid concentration is between 0.01 wt% and 100 wt%, particularly between 0.1 wt% and 10 wt%, particularly between 0.5 wt% and 5 wt%.
- the method, formulation and preservative according to the invention are characterized in that said shell comprises a polymer network, particularly an interpenetrating network, double network, and/or composite of two or more inter- or intra- cross-linked polymers, and more particularly in that said polymer network comprises a hydrophilic polymer network, particularly comprising one or more poly-electrolytes or polysaccharides selected from agar, alginate, chitosan, dextran, polyjethylene glycol), collagen, gelatin, hyaluronic acid, carrageenan, particularly Lambda-, Kappa and Lota carrageenan, fibroin, fibronectin, poly-l-lysine (PLL), cellulose, graphene, poly(ethylenimine) (PEI), poly(amidoamine) (PAA), dextran sulfate, silk, silk fibroin, pectin, locust bean gum, gellan gum, guar gum, tragacanth gum,
- the method, formulation and preservative according to the invention are characterized in that said shell comprises a bio-compatible, biodegradable and/or bio-resorbable polymer network, particularly a polymer network comprising a methyl-methacrylate derivative, a caprolactone derivative, a lactic acid derivative, a glycolic acid derivative, and/or a co-polymer of lactic acid and glycolic acid, more particularly in that said polymer network comprises a poly(lactic-co-glycolic acid), a poly(caprolactone) and/or a poly(methyl-methacrylate).
- a bio-compatible, biodegradable and/or bio-resorbable polymer network particularly a polymer network comprising a methyl-methacrylate derivative, a caprolactone derivative, a lactic acid derivative, a glycolic acid derivative, and/or a co-polymer of lactic acid and glycolic acid, more particularly in that said polymer network comprises a poly(lactic-co-glycolic acid),
- polymer network comprises a cross-linked or inter-penetrating alginate network, particularly a calcium cross-linked alginate network.
- the network may be further strengthened by incorporation of nano- or micro-particles and/or polyelectrolytes.
- the method, formulation and preservative according to the invention are characterized in that said polymer shell comprises an alginate network, particularly a sodium-, calcium- and/or a shellac reinforced alginate network.
- liquid hydrophobic material comprises at least one oil, particularly one or more oils from a group comprising: vegetable oils, such as sunflower oil, corn oil, linseed oil, canola oil, castor oil, palm oil, coconut oil, avocado oil, sweet almond oil, calophylum oil, sesame oil, olive oil, jojoba oil, soybean oil, cottonseed oil, rapeseed oil, peanut oil, flaxseed oil, borage oil, safflower oil, macro-algae oil and seaweed oil; essential oils, ethereal oils, macerated oils, triglyceride, animal oils, such as tallow fat, lanolin and marine oils, such as fish oils; synthetic oils, and neutral oils like medium chain triglyceride oils, as well as mixtures or derivatives thereof, and more particularly oils that are non-toxic and user-friendly, particularly sunflower oil or safflower oil.
- vegetable oils such as sunflower oil, corn oil, linseed oil, canola oil, castor oil,
- the method, preservative or formulation according to the invention may be characterized in that said liquid hydrophobic material comprises sunflower oil or safflower oil. More particularly, the method, preservative or formulation according to the invention may be characterized in that said liquid hydrophobic material is an oleogel comprising an oil, particularly sunflower oil or safflower oil.
- the method, preservative or formulation according to the invention is characterized in that said liquid hydrophobic material is an oleogel comprising an oil, more particularly comprising an oil with an oleic acid content higher than 10%, more particularly higher than 25%, more particularly higher than 50%, more particularly higher than 70%, even more particularly comprising high-oleic sunflower oil characterized by an oleic acid content higher than 70%.
- the oleogel may comprise an oil gelling agent at a concentration of at least 1 wt% (gelling agent to oleogel weight percentage), particularly at least 2 wt%, particularly at least 3 wt%, particularly at least 4 wt%, particularly at least 5 wt%, particularly between 1 wt% and 10 wt%, particularly between 4 wt% and 6 wt%.
- the method, preservative or formulation according to the invention may be characterized in that said oleogel retains substantial amounts of said oil, more particularly wherein said oleogel has the capacity to bind or retain more than 90% of said oil in said oleogel, particularly more than 95%, during at least 4 weeks at at least room temperature, particularly at 40 degrees Celsius.
- the capacity of said oleogel to bind said oil is also referred to as 'oil binding capacity 1 and is equal to the weight of bound oil determined after, for example, centrifugating the oil/oleogel mixture, divided by the weight of solid fat determined by, for example, pulse nuclear magnetic resonance (NMR).
- stability of said oil binding capacity may be determined by letting separate the unbound oil phase from said oleogel over time and determining the weight and/or volume ratio(s) of unbound oil and oleogel.
- ethereal, macerated and/or essential oils or waxes furthermore add favourable, pleasant organoleptic properties or therapeutic benefits to the product.
- suitable organic lipophilic compounds are for instance: immortelle, lavender, german chamomile, neroli, peppermint oil, rosemary, rose oil, tea tree oil, dwarf pine, juniper berry, roast chestnut extract, birch leaf extract, hayseed extract, ethyl acetate, camphor, menthol, rosemary extract, eucalyptus oil, cranberry oil.
- the method, formulation and preservative according to the invention are characterized in that said liquid hydrophobic material comprises at least one hydrophobic gelling agent, specifically a fatty acid, a wax, or a sterol that is provided in liquid form and that is gelled, crystallized or otherwise solidified into said micro-bodies.
- said liquid material is processed in a liquid state and allowed to solidify below a gelling temperature of the hydrophobic gelling agent to form crystals incorporated in a hydrophobic network, also referred to as oleogel.
- the suspended powder will become captured (trapped) in such stable solidified oleogel matrix that prevents migration and/or phase separation of said suspension.
- the liquid hydrophobic material may particularly comprise one or more fatty acids and/or waxes from a group comprising: paraffin wax, rice bran wax, sunflower wax, carnauba wax, candelilla wax, beeswax, microcrystalline wax, coconut wax, ozocerite wax, beta-sitosterol, gamma-oryzanol, stearic acid, palmitic acid, behenic acid, myristic acid, lauric acid, capric acid, and fatty acid derivatives, such as fatty acid esters with short chain alcohols, such as isopropyl myristate, isopropyl palmitate and isopropyl stearate and dibutyl adipate, and particularly carnuba wax.
- fatty acids and/or waxes from a group comprising: paraffin wax, rice bran wax, sunflower wax, carnauba wax, candelilla wax, beeswax, microcrystalline wax, coconut wax, ozocerite wax, beta-sito
- the gelling, gelation, melting or crystallization temperature of the oleogel and/or hydrogel may typically be not a single point, but may occur over a temperature range characterized by an onset and an offset temperature, or specifically a melting onset and melting offset temperature, a gelling onset and gelling offset temperature, or a crystallization onset and crystallization offset temperature, wherein 'onset' refers to starting and 'offset' refers to completion of the respective process.
- the solidification temperature of the liquid material can be lower than the melting/crystallization temperature, in other words, the crystallization offset temperature can be lower than the crystallization onset temperature.
- the expressions "gelation” and “solidification” and like derivatives, such as “gelled”, “gelling” and “solidified”, may be used interchangeably.
- the method, formulation and preservative according to the invention are characterized in that said oleogel comprises a hydrophilic gelling agent, in particular a polysaccharide, a (modified) starch, a protein, a natural gum, a hydrocolloid, a steroid, a hydrophilic phytosterol derivative, or a phospholipid, in particular one or more gelling agents selected from the group of cellulose, maltodextrin, dextran, hyaluronic acid, gelatin, whey protein, gum Arabic, gum tragacanth, xanthan gum, carrageenan, agar, lecithin, propylene glycol, silica (nanoparticles), more particular ethyl cellulose.
- the hydrophilic gelling agent aids in further stabilizing the suspension of said powder and said oleogel.
- fats, waxes, and oleogels are solid or creamy (malleable) at room temperature. Advantage may be taken of this natural nature of fats, waxes, and oleogels to further immobilize the active compound within the capsule. Accordingly, a further particular embodiment of the method according to the invention is characterized in that said liquid hydrophobic material is processed in a liquid condition to at least partly solidify or have solidified below a solidification temperature thereof. In a further specific embodiment the method according to the invention is characterized in that said liquid hydrophobic material is cooled down to below said solidification temperature thereof at a cooling rate faster than 0.1 K/min, particularly faster than 1 K/min, more particularly faster than 10 K/min, and more particularly faster than 100 K/min.
- the solidification temperature of the liquid material can be tuned by changing its composition, particularly the types and concentrations of oils, waxes, and other components in an oleogel.
- These wax or fat containing oleogels may be processed in a liquid form to create the micro-bodies or capsules, particularly by using the method of co-pending European patent application by the same applicant that published as EP 3.436.188 Al and whose subject matter is herewith incorporated by reference.
- the product may be stored below the oleogel gelation temperature, which could, depending on the oleogel composition, for example be at 40 degrees Celsius, room temperature, or at 4 degrees Celsius. While the oleogel contained in the capsule is in a solid state it will counteract migration of both the active compound out of the capsule as well as of environmental compounds into the capsule. Storing the micro-bodies at temperatures below the solidification temperature of the oleogel may also lead to a denser oleogel network and further strengthening of the oleogel network in time.
- the oleogel composition according to the present invention may be such that the oleogel solidification temperature is between 0 and 100 degrees Celsius, particularly between 4 and 90 degrees Celsius, particularly between 4 and 40 degrees Celsius, particularly between 20 and 40 degrees Celsius, particularly between 20 and 90 degrees Celsius, particularly between 40 and 90 degrees Celsius, particularly between 40 and 50 degrees Celsius, particularly between 50 and 60 degrees Celsius, particularly between 60 and 70 degrees Celsius, particularly between 80 and 90 degrees Celsius, and preferably above room temperature.
- a further embodiment of the method, formulation and preservative according to the invention have the feature that said oleogel has a solidification offset temperature below about 60 degrees Celsius. This suppresses thermally induced degradation of the active compound.
- Suitable candidates to formulate said oleogels are for instance a wax that is selected from a group of montan wax, carnauba wax, glycol montanate, paraffin wax, rice bran wax, sunflower wax, candelilla wax, beeswax, microcrystalline wax, coconut wax, ozocerite wax and mixtures thereof.
- the method, formulation and preservative according to the invention are characterized in that said oleogel comprises an emulsifier or plasticizer, such as fatty acids, glycolipids, monoglycerides, diglycerides, triglycerides, or phospholipids, or a mixture thereof, particularly soy lecithin or polyglycerol polyricinoleate (PGPR).
- an emulsifier or plasticizer such as fatty acids, glycolipids, monoglycerides, diglycerides, triglycerides, or phospholipids, or a mixture thereof, particularly soy lecithin or polyglycerol polyricinoleate (PGPR).
- PGPR polyglycerol polyricinoleate
- the method, formulation and preservative according to the invention are characterized in that said oleogel comprises an oil-soluble anti-oxidizing agent, such as, for example, a tocopherol (known as vitamin E), particularly alpha-tocopherol, particularly 0.01-10 wt% alpha-tocopherol in oleogel, particularly 0.1-1% alpha-tocopherol in oleogel.
- an oil-soluble anti-oxidizing agent such as, for example, a tocopherol (known as vitamin E), particularly alpha-tocopherol, particularly 0.01-10 wt% alpha-tocopherol in oleogel, particularly 0.1-1% alpha-tocopherol in oleogel.
- the method, formulation and preservative according to the invention are characterized in that said powder is provided as a dry, substantially water-free powder. Removing any initial water or water vapour will increase the lifetime of the powdery ingredient.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises an anti-oxidizing agent and/or a nutrient, particularly one or more from the group of catalase, polyphenol, curcumin, quercetin, catechin, lignan, resveratrol, citric acid, and L-ascorbic acid.
- said powder comprises L-ascorbic acid.
- the encapsulation according to the invention protects the compound from oxidative and/or pro-oxidative conditions such as moisture and oxygen from ambient air or from a liquid formulation in which the micro-bodies are mixed, thereby retaining at least a substantial part of its original nutrient and/or anti-oxidation capabilities, particularly as compared to non-encapsulated anti-oxidizing agent and/or nutrients.
- the method, formulation and preservative according to the invention are characterized in that said active compound is a hydrating agent, particularly hyaluronic acid, alginate, gelatin or collagen.
- the encapsulation according to the invention substantially shields the compound from ambient air and/or from water, thereby preventing degradation of the hydrating agent, for example through hydrolysis, thereby retaining its original structure and hydrating capabilities.
- micro-bodies that contain a water-shielding oleogel advantageously allow for the encapsulation of relatively high concentrations of hygroscopic compounds such as hydrophilic polymers, like dry hyaluronic acid powder.
- hygroscopic compounds such as hydrophilic polymers, like dry hyaluronic acid powder.
- the hygroscopic compound remains a dry, non-wetted powder that may have been blended within a molten oleogel during the encapsulation process, which enables more facile processing and easier encapsulation of higher polymer concentrations as compared to handling the hygroscopic compound that is not mixed with a oleogel.
- hydrophilic polymers can become notoriously sticky and viscous upon interaction with water or moisture, especially at relatively high molecular weights (> 100 kDa, >1000 kDa) and/or high water-binding molecules, such as, for example, high molecular weight hyaluronic acid.
- Sticky powders or high viscous solutions are difficult to process and particularly difficult to encapsulate.
- the method, formulation and preservative according to the invention are, however, characterized in that said powder comprises a hydrophilic polymer with a molecular weight larger than 10 kDa, particularly larger than 100 kDa, particularly larger than 1000 kDa, in particular a polysaccharide, in particular hyaluronic acid.
- the present invention enables encapsulation of such relatively high concentrations of hygroscopic compounds in their dry powder form by dispersing them within oleogel and substantially protecting them from contact with water or other aqueous solvents.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a hygroscopic compound, particularly a natural compound, particularly from the group of hydrophilic polymers, polysaccharides, proteins, nucleic acids, and water-soluble salts.
- a hygroscopic compound particularly a natural compound, particularly from the group of hydrophilic polymers, polysaccharides, proteins, nucleic acids, and water-soluble salts.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a hygroscopic salt, in particular a salt of a quaternary ammonium cation, more particularly a choline salt, in particular one from the group of choline chloride, choline bitartrate, choline borate, choline dihydrogen citrate, choline bicarbonate and choline chloride carbamate, even more particularly choline chloride.
- a hygroscopic salt in particular a salt of a quaternary ammonium cation
- a choline salt in particular one from the group of choline chloride, choline bitartrate, choline borate, choline dihydrogen citrate, choline bicarbonate and choline chloride carbamate, even more particularly choline chloride.
- Choline salts are used in nutrition, for example as adjuncts to animal and poultry feeds.
- the hygroscopic nature of the choline salts that are commonly available makes uniform mixing difficult and the preparation otherwise unsatisfactory.
- the salts tend to liquify, which is problematic for processing and also causes undesirable odor of the material.
- Mixing dry choline salts in liquified oleogel and subsequently encapsulating in a preserving micro-body according to the invention protects the choline against moisturization, sticking together, and deterioration.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a dried, spray dried, or freeze dried composition comprising an active ingredient (hygroscopic) drying excipient, particularly a drying excipient comprising at least one polycarbohydrate, monosaccharide, disaccharide, or polysaccharide compound, and more particularly a drying excipient being a sugar, more particularly the drying excipient being selected from the group of dextran, dextrin, maltodextrin, trehalose, lactose, glucose, dextrose, sucrose, fructose, maltose, isomaltose, sorbitol, mannitol, lactitol, xylitol, and/or erythritol.
- an active ingredient hygroscopic drying excipient
- a drying excipient comprising at least one polycarbohydrate, monosaccharide, disaccharide, or polysaccharide compound
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a biological compound, particularly an organism, a protein, an enzyme, a peptide, a nucleotide, or a mixture thereof.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a viable compound, particularly a living cell, more particularly a bacteria or microbiota.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises one or more sensitive bacteria selected from the group of anaerobic bacteria, non-spore forming bacteria, and other bacteria sensitive to moisture, acid, heat, and/or oxygen.
- said preserving micro-bodies at least partially protects said sensitive bacteria and thereby increase the survival of the bacteria during and/or after the production process and/or extend the shelf life of a product.
- said active compound, particularly said sensitive bacteria are more stable and have a higher viability during and after production of a product if said active compound, particularly said sensitive bacteria are encapsulated in said preserving micro-bodies as compared to said active compound, particularly said sensitive bacteria that are not encapsulated in said preserving micro-bodies.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises one or more bacteria from a group of Bacteroides, Bifidobacterium, Fusobacterium, Bacillus, Lactobacillus, Saccharomyces, Streptococcus, Enterococcus Porphyromonas, Prevotella, Actinomyces, Propionibacterium, Clostridia, particularly one or more from the group of Bifidobacterium bifidum, Bifidobacterium lactis, Bifidobacterium adolescentis, Bifidobacterium breve, Bifidobacterium infantis, Bifidobacterium longum, Lactobacillus acidophilus, Lactobacillus rhamnosus, Saccharomyces boulardii, Lactobacillus plantarum, Streptococcus thermophilus, Lactobacillus casei, Lactobacillus para
- the method, formulation and preservative according to the invention are characterized in that said powder comprises one or more anaerobic bacteria from the group of Bacteroides, Bifidobacterium, Fusobacterium, Porphyromonas, Prevotella, Actinomyces, Propionibacterium, Clostridia, particularly one or more from the group of Bifidobacterium bifidum, Bifidobacterium lactis, Bifidobacterium adolescentis, Bifidobacterium breve, Bifidobacterium infantis, and Bifidobacterium longum.
- Bacteroides Bifidobacterium, Fusobacterium, Porphyromonas, Prevotella, Actinomyces, Propionibacterium, Clostridia, particularly one or more from the group of Bifidobacterium bifidum, Bifidobacterium lactis, Bifidobacterium a
- the method, formulation and preservative according to the invention are characterized in that said powder comprises one or so called 'next-generation probiotics', more particularly said powder comprises one or more next-generation probiotics from the group of Akkermansia muciniphila, Faecalibacterium prausnitzii, Bacteroides thetaiotaomicron, Bacteroides fragilis, Roseburia spp., Prevotella spp., Alistipes spp., Christensenella minuta, Blautia spp., Eubacterium hallii, and Methanobrevibacter smithii
- the method, formulation and preservative according to the invention are characterized in that said powder comprises one ore more prebiotics, particularly one ore more from the group of oligosaccharides, fructans, galactans, starch, pectins, and beta-glucans.
- prebiotics are also referred to as dietary fibers.
- the method according to the invention is characterized in that said liquid hydrophobic material is solidified by combining the micro-bodies with a phase, particularly a liquid phase, that has a temperature lower than a solidification temperature of said liquid hydrophobic material, particularly a temperature below room temperature, more particularly a temperature below 10 degrees Celsius.
- said phase comprises a liquid phase containing a cross-linking compound to cross-link said shell polymer.
- micro-bodies may be encapsulated by combining a liquid stream containing said cross-linking compound with a stream of said micro-bodies, particularly by using the method of a co-pending European patent application by applicant that published as EP 3.436.188 Al whose subject matter is herewith incorporated by reference.
- the method according to the invention are characterized in that said liquid phase has a temperature that induces thermal or physical cross-linking of at least on of said shell polymers.
- the micro-bodies may stored in a carrier liquid at a temperature above a freezing temperature of the said carrier liquid and below said oleogel solidification temperature, particularly below room temperature, particularly below 10 degrees Celsius, particularly at approximately 4 degrees Celsius.
- the method, formulation and preservative according to the invention are characterized in that said powder comprises a catalyst, in particular one or more compounds from a group of compounds that catalyse amino cross-linking, particularly comprising p-TSA (para-Toluene
- DNNDSA Di Nonyl Naphtalene Di Sulfonic Acid
- DDBSA Do Decyl Benzene Sulfonic Acid
- DNNSA Di Nonyl Naphtalene mono Sulfonic Acid
- Phosphate Acid and Carboxylic Acid
- catalyze urethane cross-linking particularly including DBTL (Di Butyl Tin Laurate), DOTL (Di Octyl Tin Laurate), DBTO (Di Butyl Tin Oxide), Bismuth-based catalyst, Zirconium-based catalyst, and amine-based catalyst.
- the method according to the invention is characterized in that said one or more micro-bodies are laden with a hydrophobic compound by immersing said one or more micro-bodies into a solution of said hydrophobic compound, particularly a concentrated solution, allowing said hydrophobic compound to diffuse trough said shell into said one or more cores of said one or more micro-bodies.
- the method according to the invention is characterized in that said one or more micro-bodies are laden with a hydrophobic compound by providing said one or more micro-bodies with one or more cores in molten state prior to immersing said one or more micro-bodies into a solution of said hydrophobic compound, particularly a concentrated solution, to allow said hydrophobic compound to diffuse into said one or more cores of said one or more micro-bodies in said molten state, and subsequently allowing said one or more cores to at least substantially solidify.
- the cores may for instance comprise a molten oil or wax. After such core is solidified again, for instance by re/gelling, the hydrophobic compound will be trapped in the micro-bodies.
- the method according to the invention is characterized in that said shell comprises a calcium-alginate network that is weakened or completely removed prior to or during final application, particularly by scavenging calcium ions and at least partly disrupting the calcium-alginate network of the shell, more particularly by introducing a chelator agent such as citric acid or ethylene- diamine-tetra-acetic acid (EDTA).
- a chelator agent such as citric acid or ethylene- diamine-tetra-acetic acid (EDTA).
- the method according to the invention is characterized in that said micro-bodies are dried, particularly by a drying method chosen from a group containing evaporation, blowing dry gas, vacuum drying, fluid bed drying, freeze drying, microwave drying, and chemical drying. Such method will remove water from the micro-bodies and in particular from the hydrophilic shell.
- dry or dried micro-bodies are formed into at least par of a free flowing powder.
- the method, formulation and preservative according to the invention are characterized in that said active component has organoleptic properties that are masked by said at least one core inside said micro-body. The organoleptic properties may relate to either a taste or a smell.
- said active component is a fragrance, perfume or a mixture of smelling compounds.
- said active component is a flavor or mixture of tasty compounds.
- said active component is a bad-tasting and/or bad-smelling compound of which the taste and/or smell is at least partially masked by the method, formulation, and/or preservative according to the invention.
- a formulation comprising an active compound in a preserved state by means of the preservative according to the invention is characterized in that said formulation is a product or intermediate product for a cosmetic, a dermatological, food, nutritional, supplemental, agrochemical, fragrance, pharmaceutical, (bio)medical, household, energy storage, coating, or adhesives/glue application.
- said formulation or said (intermediate) product is of detrimental nature to the pristine (i.e., unpreserved) active compound, more particularly characterized in that said formulation or said (intermediate) product comprises substantial amounts of water, more particularly >30 wt% water, more particularly >50 wt% water.
- said formulation or said (intermediate) product is of detrimental nature to the pristine (i.e., unpreserved) active compound, more particularly characterized in that said formulation or said (intermediate) product has an acidic pH ⁇ 7, more particularly pH ⁇ 4. More particularly, the product is selected from the group of creams, lotions, serums, gels, shampoos, beverages, drinks, soda drinks, gummies, bars, tablets, capsules, pills, dairy, and injectables.
- a formulation comprising an active compound in a preserved state by means of the preservative according to the invention is characterized in that said formulation is a product or intermediate product produced via a process that is damaging or detrimental to said active compound (especially when said active compound is not in said preserved state), more particularly wherein said process comprises one or more process steps performed at or above room temperature, more particularly at or above 40 degrees Celsius, more particularly at or above 60 degrees Celsius, more particularly at ore above 80 degrees Celsius, more particularly wherein one or more process steps are related to spray drying, hot melt, extrusion, injection molding, more particularly wherein the process involves one or more steps involving shear forces (e,g., mixing, blending, injection, extrusion, or centrifugation), and more particularly wherein the process is related to the production of (edible) gummies, also referred to as gummification.
- said process comprises one or more process steps performed at or above room temperature, more particularly at or above 40 degrees Celsius, more particularly at or above 60 degrees Celsius, more particularly at ore above 80 degrees Celsius, more particularly
- the invention moreover relates to a cosmetic product, a personal care product or home care product, a dermatological product, a food or nutrition product, an agrochemical product, a fragrance product, a health or healthy product, a pharmaceutical product, a (bio)medical product, a household product, an energy storage product, a coatings product, and to an adhesives product that comprises the above formulation with an active compound in preserved form.
- Figure 1 shows exemplary images of phase separation of an LAA-laden oleogel at different wax fractions
- FIG. 2 gives a quantification of the phase separation shown in figure 1;
- Figure 3 shows visual aspects of multiple capsules mixed with an aqueous base liquid
- Figure 4 shows a schematic representation of a micro-droplet encapsulated by a polymer shell according to the invention
- Figure 5 shows viable and multiplying probiotic cells expressed in colony-forming units (CFU) per 1 gram of the original excipient material after 1, 5, and 13 weeks, respectively, on stability tests in comparison to non-encapsulated probiotics in water and exposed to environmental air at 25 degrees Celsius (N.D. indicates not detectable);
- CFU colony-forming units
- Figure 6 shows a graph of a comparison of the stability of encapsulated probiotic L. Rhamnosus over time during accelerated stability tests in the following core formulations:
- PB beads 1 5% carnauba oleogel in safflower oil; probiotic powder dispersed directly into oleogel at 45°C;
- PB beads 2 5% carnauba oleogel in safflower oil; probiotic powder in oil mixed in a 1:1 ratio into oleogel at 50°C;
- PB beads 3 5% candelilla oleogel in safflower oil; probiotic powder dispersed directly into oleogel at 45°C; and
- the viable and multiplying probiotic cells are expressed in colony-forming units (CFU) per 1 gram of the original excipient material after 13 weeks of stability tests.
- CFU colony-forming units
- Figure 7 shows relative anti-oxidant activities of encapsulated versus unencapsulated active LAA under different stability test conditions in time.
- FIG 4 shows a schematic representation of a preservative according to the invention.
- the preservative comprises one or more micro-bodies as shown in the figure that are encapsulated by a polymer shell according to the invention.
- the micro-body comprises a core 10,20 surrounded by a shell 30.
- the shell 30 is formed by a polymer network.
- Said core 10,20 comprises an at least substantially solidified, particularly gelled, gellable or crystallizable liquid hydrophobic material 20, particularly an oleogel.
- a solid powder 10 is dispersed throughout said oleogel 20 and comprises said active compound.
- the micro-body or micro-droplet according to the invention can be realised in a wide range of dimensions, ranging from sub-micron like nano proportions to a few millimetre.
- the application of the active compound has been found particularly favourable, if provided in the form of such micro or nano micro-bodies, having sub-micron to millimetre size.
- said shell layer 30 may enclose a volume of between the order of one femtolitre and the order of one to several millilitres.
- the micro-droplet 10,20,30 has a diameter of the order of between half a micron and a centimetre, particularly between 5 micron and 5 millimetre, particularly between 100 and 500 micron, even more particularly between 150 and 350 micron, between 500 and 5000 micron, between 1 and 5 millimetre or between 2 and 4 millimetre.
- the micro-bodies may be substantially spherical, having a sphericity of over 0.8, particularly beyond 0.9, and more particularly exceeding 0.95.
- the micro-body or microdroplet may, however, be not perfectly spherical, its diameter being represented by its average Feret diameter determined using, for instance, microscopic or macroscopic imaging in combination with dynamic or static image analysis. Alternatively, the diameter may be determined using laser diffraction, dynamic ultrasonic extinction, or dynamic light scattering.
- the sphericity of the micro-bodies may be described as circularity.
- the micro-bodies may be substantially circular, having a circularity of over 0.8, particularly beyond 0.9, and more particularly exceeding 0.95.
- Sphericity of a particle can be calculated by (n A l/3 (6 Vp) A 2/3) / Ap, wherein Vp is the particle's volume, Ap is the particle's surface area, and a perfect sphere is valued by a sphericity of exactly one.
- Circularity of a particle can be calculated by 4 n (area/perimeter A 2), wherein a perfect circle is valued by a circularity of one.
- the micro-bodies have a substantially identical size within a size distribution (dispersity) showing a relative size distribution characterized as coefficient of variation (i.e., standard deviation divided by average) lower than 10%, particularly lower than 7.5%, more particularly lower than 5%. Relative size distributions lower than 10% will be called 'mono-disperse 1 .
- the suspension 20 may contain said powder 10 at a concentration higher than 0.01% weight/weight (wt%), particularly between higher than 1 wt%, particularly higher than 10 wt%, particularly between 0.01 and 65%, particularly 0.1-50 wt%, particularly 0.5-5 wt%, particularly 5-40 wt%, particularly 5-15 wt%, particularly approximately 10 wt%.
- a moisture content of said suspension may be lower than 40%, particularly lower than 30%, particularly lower than 20%, particularly lower than 10%.
- a moisture content of the suspension may be lower than 40%, particularly lower than 30%, particularly lower than 20%, particularly lower than 10%.
- the water activity (aw) of said oleogel may be lower than 0.7, particularly lower than 0.6, particularly lower than 0.5, particularly lower than 0.4, particularly lower than 0.3, particularly lower than 0.2, particularly lower than 0.1.
- the water activity (aw) is the partial vapour pressure of water in a solution divided by the standard state partial vapour pressure of water.
- the water activity (aw) of the oleogel may be lower than 0.7, particularly lower than 0.6, particularly lower than 0.5, particularly lower than 0.4, particularly lower than 0.3, particularly lower than 0.2, particularly lower than 0.1.
- LAA-laden oleogel by incubating the suspension at 4 °C for at least 1 hour.
- the stability of the LAA-laden oleogel systems was determined by measuring the relative amount of phase separation after 28 days incubation at 40 °C and > 80% humidity.
- Carnauba wax concentrations of 2.5 wt% (A), 3.5 wt% (B), 4.5 wt% (C and D), and 5.5 wt% (E) in sunflower oil where compared.
- LAA concentrations where varied from 10 wt% to 40 wt% in oleogel.
- Figure 1 (representative images) and Figure 2 (quantification of phase separation) clearly show that suspensions B-E that comprise over 3 wt% wax are significant more stable after 28 days at 40 °C and > 80% humidity than suspension A having less than 3% wt% wax.
- oleogel 340 g sunflower oil was heated to 100 to 110 °C, after which 20 g candelilla wax was added. The mixture was mixed until the wax melted and then kept at 100 to 110 °C for 10 to 15 minutes. The mixture was cooled down to 60 °C while stirring. Then 40 g LAA was slowly added to the wax/oil mixture while mixing at 2500 rpm using an overhead stirrer.
- the mixture was stirred for at least 5 minutes at 2500 and subsequently 15 minutes at 2000 rpm while the temperature was kept between 50 and 60 °C.
- the LAA/wax/oil mixture was then further homogenized using a rotor-stator mixer (ultra-turrax) at 16000 rpm for 5 min using mixer intervals of 1 to 2 min to prevent the temperature from increasing above 60 °C. Between homogenization intervals, the mixture was continuously mixed by gentle agitation to keep a homogeneous suspension.
- the LAA/wax/oil suspension was kept between 50 and 60 °C at al times and until further use (i.e., encapsulation).
- Capsules were produced with a dripping set-up using two syringe pumps and a coaxial nozzle, comprising an inner channel co-axially surrounded by an annular outer channel.
- Another syringe (also prewarmed to at least 50 °C) was filled with a solution containing 0.75 wt% sodium alginate (SA), 0.5 wt% agar, and 0.5 wt% carboxy methyl cellulose (CMC) in water and connected via heat-traced tubing (set to at least 50 °C) to the outer annulus of the coaxial nozzle.
- SA sodium alginate
- CMC carboxy methyl cellulose
- the syringes were emptied using a syringes pump that created a steady stream of compound liquid exiting the coaxial nozzle and pinching off into compound core-shell miucro-bodies comprising a core of LAA/wax/oil suspension and a shell of SA/agar/CMC solution.
- the falling miucro-bodies (due to gravity) were collected in an ice-cooled and continuously stirred bath with cross-linker solution comprising 0.2 M calcium chloride and 20 v/v% ethanol. After at least 15 minutes incubation, the cross-linked capsules were transferred to cross-linker liquid with calcium chloride (without ethanol) and stored at 4 °C overnight, which allowed the oleogel cores to further gel.
- capsule production method was explored, using similar core and shell liquids (i.e., 20 wt% LAA / 5.0 wt% carnauba wax in sunflower oil suspension as the core liquid, and 0.75% SA / 0.5 wt% agar solution as the shell liquid).
- capsules were produced using 'in-air microfluidics 1 , as described in WO 2017/167798, using a heat-traced co-axial first nozzle set to at least 50 °C and a simple (single opening) second nozzle.
- the core and shell liquids were jetted from the heated co-axial nozzle, while cross-linker solution containing 0.2 M calcium chloride + 20 v/v% ethanol, was jetted from the second nozzle.
- the liquid core/shell compound jet (with active/oil/wax dispersion in the core and hydrophylic polymer solution in the shell) was broken into substantially identical miucro-bodies.
- Such monodisperse compound droplet train or jet stream may typically be composed of substantially equally sized miucro-bodies with typically a coefficient of variation in size or diameter, i.e. a standard deviation divided by average, of less than 10%.
- the stream of compound core-shell miucro-bodies (which were approximately 50 to 60 °C) was coalesced with the liquid jet containing cross-linker that was kept at approximately 4 °C, which caused the (partial) solidification of the shell via (physically or chemically) cross-linking the polymers in the shell, thereby forming SA/agar/CMC capsules with a core containing dry LAA powder suspended in a gelling oil/wax mixture.
- the coalesced miucro-bodies and jets were collected in a bath with ice-cold cross-linker liquid comprising 20% ethanol and 0.2 M calcium chloride.
- Some capsules were post-treated with 1 wt% citric acid, which can cross-link the CMC, but can also act as plasticizer for the calcium-alginate polymer network, altogether increasing the mechanical stability and yield stress of the capsules.
- the resulting capsules were mixed with another aqueous phase and the product stability was analysed by evaluating the appearance and color of the samples at several time points during accelerated stability testing at 40 °C and 60 °C and >80% humidity.
- Figure 3 shows the visual aspect of multiple capsules mixed with an aqueous base liquid after 28 days of accelerated stability test (40 °C and >80% humidity).
- the left sample ( Figure 3A,3B) contains capsules that have a shell comprising calcium-cross-linked sodium alginate and cores comprising 10 wt% dry LAA powder dispersed in oleogel consisting of 5 wt% carnauba wax in sunflower oil.
- the right sample ( Figure 3C,3D) contains capsules that have a shell comprising calcium-cross-linked sodium alginate similar to the capsules in the left sample, and a core comprising carnauba-wax stabilized W/O emulsion including 10% LAA dissolved in the water phase.
- These capsules ( Figure 3C,3D) have been prepared according to the method and design as described in International patent application WO2022/029623 by applicant.
- Capsules were prepared similarly to the method in example 3, but using different core and shell liquids. Instead, the core composition contained 1 wt% probiotics (spray dried powder comprising mixed strains) suspended in a mixture of 4 wt% candelilla wax in sunflower oil, instead of LAA in carnauba wax / sunflower oil mixture.
- probiotics spray dried powder comprising mixed strains
- Capsules were prepared similarly to the method in example 3, but using different core and shell liquids.
- the core composition contained 2 wt% non-spore forming probiotics (freeze dried Lactobacillus rhamnosus) suspended in a mixture of 5 wt% carnauba wax in safflower oil, instead of LAA in carnauba wax / sunflower oil mixture, and the shell comprising 1.5wt% SA, instead of SA/agar mixture.
- probiotic-laden capsules were subjected to stability tests, during which the capsules were incubated in calcium-containing aqueous medium at 25°C. At predefined time points (after 1, 5, 13 weeks), probiotics were extracted from the capsules using shear homogenization, inoculated on agar plates, and incubated for 48 hours at 37°C. The number of viable and multiplying probiotic cells was assessed through colony-forming unit (CFU) enumeration.
- CFU colony-forming unit
- capsule formulation according to the invention offers protective properties against, amongst others, water, moisture and non-chilled (i.e., heat) conditions, which are indeed critical factors known to compromise probiotic viability.
- Bi-gel capsules were prepared similarly to the method in example 3, but using different core and shell liquids.
- the core composition contained 2 wt% non-spore forming probiotics (freeze dried Lactobacillus rhamnosus) suspended in a mixture of 5 wt% carnauba wax in safflower oil, instead of LAA in carnauba wax / sunflower oil mixture, and the shell comprising 1.5wt% SA, instead of SA/agar mixture.
- the capsules where successfully dried by using a fluidized bed drier set at 35°C air inflow temperature (i.e., below melting point of oleogel) in the presence of 2 wt% aluminium silicate (used as anticaking agent) until a free-flowing powder was obtained.
- Viability analysis of extracted probiotics in combination with CFU counting revealed that "90% of probiotics survived the drying process.
- Capsules were prepared similarly to the method in example 3, but using different core and shell liquids.
- the core composition contains 2 wt% probiotics (freeze dried L. rhamnosus) suspended in a mixture of 5 wt% in carnauba wax in safflower oil instead of LAA in carnauba wax / sunflower oil mixture, and the shell comprising 1.5wt% SA, instead of SA/agar mixture, shown as "PB beads 1" in figure 6.
- probiotics freeze dried L. rhamnosus
- the wax/oil mixture was first heated to 90-100 degrees Celsius to form a transparent and homogeneous liquid, and then cooled down to 45 degrees Celsius before probiotics containing powder was added and mixed through.
- capsules with the same composition as PB beads 1 were made using a different core liquid preparation method that resulted in a less homogeneous distribution of wax throughout the oleogel core, shown as "PB beads 2" in figure 6.
- PB beads 2 a 10% carnauba wax/safflower oil mixture without probiotics was heated to 90-100 degrees Celsius and then cooled to 50 degrees Celsius, after which probiotics-laden oil at room temperature (i.e., "20-25 degrees Celsius) was added in a 1:1 ratio to reach a final carnauba concentration of 5%. Blending the warmer wax/oil mixture with the colder probiotics-laden oil presumably resulted in substantial wax crystallization and oleogelation prior to the in-air microfluidics encapsulation process, and eventually resulting in a less homogeneous and less protective oleogel network surround the probiotics.
- room temperature i.e., "20-25 degrees Celsius
- probiotics-laden capsules was prepared in a similar manner as PB beads 1, but then the core composition contained probiotics in a mixture of 4 wt% candelilla wax in safflower oil, shown as "PB beads 3" in figure 6.
- Microcapsules were prepared similarly to the method in example 3, but using different core and shell liquids. Instead, the core composition comprised 10wt% LAA and 5wt% Carnauba wax in high-oleic sunflower oil and the shell composition comprised (gelled) SA/agar/CMC.
- the capsules were provided as a 50-60% slurry in an aqueous medium in a wide-neck high-density polyethylene container and subsequently subjected to and passed a transportation test according to ASTM D4169-16 before being put on stability tests.
- the capsules were retrieved from the container, separated from the aqueous transport medium by sieving, blended into a various water-based liquids and gels, and subjected to different storage conditions at 4, 21, 30, 40, and 60 ⁇ 2 degrees Celsius for a minimum of 3 months.
- LAA was extracted from the capsules using ultrasonic treatment in ethanol and anti-oxidant activity of the extracted LAA was measured using the 2,2-diphenyl-l-picrylhydrazyl assay in combination with spectrophotometry.
- the encapsulated active LAA shows significantly higher anti-oxidant activity and slower reduction of anti-oxidant activity, as well as longer anti-oxidant half-life time of anti-oxidant activity as compared to unencapsulated active LAA (i.e., control) ( Figure 7).
- the method, formulation and preservative according to the invention may be used in embodiments, wherein said active compound comprises at least one vitamin, particularly a vitamin that is selected from a group containing thiamine, riboflavin, nicotinic acid, pantothenic acid, pyridoxine, biotin, folic acid, cyanocobalamin, lipoic acid, ascorbic acid, lecithin, glycyrrhizin acid, retinol, retinol palmitate, tocopherol, tocopherol acetate, salicylic acid, benzoyl peroxide, and azelaic acid and/or derivatives thereof, more particularly ascorbic acid and/or derivatives thereof.
- said active compound comprises at least one anti-oxidant, particularly an anti-oxidant that is selected from a group containing poly-phenols, thiol-based components, sulphite and derivatives thereof.
- the active compound may be used, for instance, as nutritious supplement or for pharmaceutical treatment, in which case it is likely to be administered orally.
- the shell layer may be formulated to survive the acidic environment of the human stomach to be digested in the more downstream portion of gastrointestinal tract of the user to release its contents.
- the shell layer may comprise a digestible or fermentable polymer, more particularly the shell layer may comprise a pectin compound.
- pro- and prebiotics may be administered particularly effectively in this manner.
- said shell layer may carry a coating, preferably an edible coating, particularly a hydrophobic coating containing nano-particles or a wax like carnauba wax.
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| US6534091B1 (en) * | 1999-07-02 | 2003-03-18 | Cognis Iberia S. L. | Microcapsules |
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| US20220265527A1 (en) * | 2019-09-24 | 2022-08-25 | Gpcp Ip Holdings Llc | Microencapsulated probiotic and compositions containing the same |
-
2023
- 2023-04-14 NL NL2034584A patent/NL2034584B1/en active
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2024
- 2024-04-12 WO PCT/IB2024/053608 patent/WO2024214063A1/en active Pending
- 2024-04-12 CN CN202480025693.1A patent/CN121152674A/en active Pending
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