COATED MICROCAPSULES AND METHODS FOR THE PRODUCTION THEREOF

Abstract

A method of producing coated microcapsules comprises the steps of producing microcapsules by cold gelation having a denatured or hydrolysed protein matrix and an active agent contained within the matrix, and drying the microcapsules. A meltable coating composition comprising wax and oil and configured to have a melting point of about 70° C. to about 100° C. is heated to a temperature above the melting point of the meltable coating composition to melt the meltable coating composition, and the microcapsules are coated with the melted meltable coating composition

Claims

1. A method of producing coated microcapsules comprising the steps of: producing cold-gelated microcapsules having an average diameter of 50-500 microns and a denatured or hydrolysed protein matrix and an active agent contained within the matrix; drying the microcapsules; providing a meltable coating composition comprising wax and oil having a melting point of 70-100° C.; heating the meltable coating composition to a temperature above the melting point of the meltable coating composition to melt the meltable coating composition; and coating the microcapsules with the melted meltable coating composition.

2. A method according to claim 1, in which the coating composition comprises 50-90% wax and 10-50% oil.

3. A method according to claim 1 or 2, in which the coating composition comprises 60-70% wax and 30-40% oil.

4. A method according to any preceding Claim, in which the protein is denatured protein.

5. A method according to any preceding Claim in which the matrix consists essentially of polymerised protein.

6. A method according to any preceding Claim, in which the wax comprises carnauba wax.

7. A method according to any preceding Claim, in which the oil comprises coconut oil.

8. A method according to any preceding Claim in which the coating composition comprises carnauba wax and beeswax or coconut oil.

9. A method according to any preceding Claim in which the coating composition comprises carnauba wax, beeswax, and coconut oil.

10. A method according to any preceding Claim, in which the drying step comprises drying the microcapsules to water activity a.sub.w of less than 0.3 at 25° C.

11. A method according to any preceding Claim, in which the drying step comprises drying the microcapsules to water activity a.sub.w of less than 0.2 at 25° C.

12. A method according to any preceding Claim, in which the drying step comprises a primary drying stage and a secondary drying stage in a low humidity environment.

13. A method according to any preceding Claim, in which the coating step comprises mixing the heated coating composition and dried microcapsules in a coating chamber until the coating composition has coated the microcapsules and solidified.

14. A method according to any of claims 1 to 12, in which the coating step comprises spraying the heated coating comprising on to the dried microcapsules on a fluidised bed.

15. A method according to claim 13 or 14, in which the heated coating composition is homogenised at high shear prior to coating the microcapsules.

16. A method according to any preceding Claim, in which the coating step employs about 40-60% coating composition and about 40-60% dried microcapsules.

17. A method according to any preceding Claim, in which the matrix comprises denatured vegetable or milk protein.

18. A method according to any preceding Claim, in which the active agent comprises a probiotic bacteria, oil, or micronutrient composition.

19. A method according to any preceding Claim, in which the microcapsules are produced by extruding microdroplets comprising denatured or hydrolysed protein and an active agent into a gelation bath, and gelation of the microdroplets in the gelation bath to provide microcapsules.

20. A method according to claim 19, in which the microcapsules are multinuclear, in which the microcapsules are produced by providing a suspension comprising denatured or hydrolysed protein matrix and an active agent, and extruding microdroplets of the suspension into a gelation bath.

21. A method according to any of claims 1 to 18, in which the microcapsules are mononuclear, in which the microcapsules are produced by providing a first liquid composition comprising denatured or hydrolysed protein matrix and a second liquid composition comprising an active agent, and co-extruding the first and second liquid compositions using concentric nozzles in which the first liquid composition is extruded through an outer nozzle and the second liquid composition is extruded through an inner nozzle to form core-shell microdroplets, and gelation of the core-shell microdroplets in a gelation bath.

22. A method according to any of claims 1 to 18, in which the microcapsules are produced by providing a first liquid composition comprising denatured or hydrolysed protein matrix and an active agent, and co-extruding the first liquid compositions and the meltable coating composition using concentric nozzles in which the first liquid composition is extruded through an inner nozzle and the second liquid composition is extruded through an outer nozzle to form core-shell microdroplets in which the shell comprises the meltable coating composition, and gelation of the core-shell microdroplets in a gelation bath.

23. A microcapsule comprising: a crosslinked denatured or hydrolysed protein matrix; an active agent contained within the matrix; wherein the microcapsule is coated with a coating composition comprising wax and oil and having a melting point of 70-100° C.

24. A microcapsule according to claim 23, in which the coating composition comprises 50-90% wax and 10-50% oil.

25. A microcapsule according to claim 24, in which the coating composition comprises 60-70% wax and 30-40% oil.

26. A microcapsule according to any of claims 23 to 25, in which the protein is denatured protein.

27. A microcapsule according to any of claims 23 to 26, in which the wax comprises carnauba wax.

28. A microcapsule according to any of claims 23 to 27, in which the wax comprises beeswax and/or carnauba wax.

29. A microcapsule according to any of claims 23 to 28, in which the oil comprises coconut oil.

30. A microcapsule according to any of claims 23 to 29, in which the coating composition comprises carnauba wax and beeswax or coconut oil.

31. A microcapsule according to any of claims 23 to 29, in which the wax comprises carnauba wax, beeswax, and coconut oil.

32. A microcapsule according to any of claims 23 to 31, in which the microcapsule has a water activity Aw of less than 0.3 at 25° C.

33. A microcapsule according to any of claims 23 to 32, in which the microcapsule has a water activity Aw of less than 0.2 at 25° C.

34. A microcapsule according to any of claims 23 to 33, in which the microcapsule is a mononuclear microcapsule.

35. A microcapsule according to any of claims 23 to 33, in which the microcapsule is a multinuclear microcapsule.

36. A microcapsule according to any of claims 23 to 35, in which the protein is selected from a milk or vegetable protein, which is denatured.

37. A heat-treated composition comprising microcapsules according to any of claims 23 to 36, in which the composition is heat treated at a temperature less than the melting point of the coating composition.

38. A heat-treated composition according to claim 37 which is pasteurised.

39. A method of making a heat-treated composition comprising the steps of providing a composition comprising microcapsules according to any of claims 23 to 36, and heat treating the composition at a temperature less than the melting point of the coating composition.

40. A method according to claim 39, in which the heat treatment is pasteurisation.

41. A heat treated composition according to claim 37 or 38, or a method according to claim 39 or 40, in which the active agent comprises probiotic bacteria.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0110] FIG. 1 . Images dry oil/wax coated microparticles. Image A shows microparticles after production (×100 magnification). Image B shows microparticles in water after 48 hours (×100 magnification). No difference recognised in surface topography after dispersion/immersion in water after 48 hour; and not water absorption recognised.

[0111] FIG. 2 . Images A and B show cold gelated microparticles before oil/wax coating application. Image B shows micro-capsules after oil+wax coating application. Images C and D show cold gelated microbeads coated with oil and wax in different proportions but not visual difference and no size difference.

[0112] FIG. 3. Image A confirms the presence of the live probiotic bacteria load in dry oil/wax coated microparticles. Cell counts can range from 1 billion to 100 billion CFU per gram and the process is sustained reproduction capacity from batch to batch. FIG. 3B shows dried oil/wax coated microparticles after high humidity storage 75% (A) and after fortification in a UHT beverage for 3 months (C). Microscopy shows no change in surface topography after stress exposure to humidity or UHT beverage environments.

[0113] FIG. 4. Microscopy images to verify the natural human digestion of coated micro-capsules during in vitro human digestion. Image 4A represented digesta after stomach incubation step. Image 4B illustrates digestion after 15 minutes intestinal incubation. Image 4C illustrates break down after 30 minute intestinal digestion and image 4D illustrates full break down after 45 minute intestinal digestion.

[0114] FIG. 5. Humidity measurements of control and coated microcapsules after 7.5 days at 75% high humidity. Dashed line represents control (porous microbeads) and continuous line represents coated microbeads that resist humidity and moisture update.

[0115] NOTE: The gain in weight while storing the samples at high relative humidity atmosphere is linked with the affinity with water. Hence, a low water gain in the samples during exposure to high humidity will correspond with those samples with highest hydrophobic profile i.e. microcapsules with a coating of oil and/or wax.

[0116] FIG. 6A. Humidity measurements of control (porous) microbeads and various coated microcapsules after storage at 75% high humidity. Different percent coatings and different ratios of oil-wax coating will generate different levels of resistance to high humidity environments.

[0117] FIG. 6B shows the comparison of weight gain vs. moisture uptake values for control microbeads and various other wax coated microcapsules after exposure to 75% high humidity. Different percent coatings and different ratios of oil-wax will generate different levels of resistance to high humidity environments.

[0118] FIG. 6C illustrates the difference humidity resistance between the control (porous)beads (high level single blue line) after 33 days at 75% high humidity using various coating combinations and coating ingredient ratios (all other coloured lines). A significant increase in moisture resistance is evident after 33 days when a coating layer is applied.

[0119] FIG. 6D compare the weight gain and moisture for various coated microparticles relative the control porous microbeads after 3.3 days storage at 75% relative humidity.

[0120] FIG. 7. Explanation for coating principle. NOTE: Generation of hydrophobic coating on cold gelated microparticles or microbeads, should have a small contact angle to ensure even coverage and continuous coating with no porous formation on the surface of the final product; and a high contact angle of water on the surface of the coating, to assure the repelling of water molecules. The values highlighted in red do not provide useful information since the contact angle in between formulation is not of relevance. However, it gives useful information in terms of compatibility. All formulations are water based but using hydrophobic polymers. This means that they will be more compatible with the simulated coating than pure water, due to the presence in dispersion of hydrophobic compounds. Accordingly, pure water showed higher contact angle onto the simulated coating, than all the formulations. Regarding the contact angle onto a glass slide, as expected, water shows the lowest contact angle corresponding with the highest wettability degree. The closest to this value will mean the highest suitability for a film-forming ability, and the generation of a continuous coating with no porous. However, this value can be affected by the viscosity of the sample, increasing the contact angle due to a higher viscosity of the formulation.

[0121] FIG. 8. Data generated from UHT trials using microcapsules loaded with probiotics and exposed to UHT process of 140° C. for 3 seconds. Free bacteria are unable to survive this process.

[0122] FIG. 9. Image A illustrates UHT beverage background with evidence of high protein and fat content as per the staining protocol used. Image B and C identifies intact beads after UHT processing. Image D shows the protein and oil-stained microbeads.

DETAILED DESCRIPTION OF THE INVENTION

[0123] All publications, patents, patent applications and other references mentioned herein are hereby incorporated by reference in their entireties for all purposes as if each individual publication, patent or patent application were specifically and individually indicated to be incorporated by reference and the content thereof recited in full.

[0124] Definitions and general preferences

[0125] Where used herein and unless specifically indicated otherwise, the following terms are intended to have the following meanings in addition to any broader (or narrower) meanings the terms might enjoy in the art:

[0126] Unless otherwise required by context, the use herein of the singular is to be read to include the plural and vice versa. The term “a” or “an” used in relation to an entity is to be read to refer to one or more of that entity. As such, the terms “a” (or “an”), “one or more,” and “at least one” are used interchangeably herein.

[0127] As used herein, the term “comprise,” or variations thereof such as “comprises” or “comprising,” are to be read to indicate the inclusion of any recited integer (e.g. a feature, element, characteristic, property, method/process step or limitation) or group of integers (e.g. features, element, characteristics, properties, method/process steps or limitations) but not the exclusion of any other integer or group of integers. Thus, as used herein the term “comprising” is inclusive or open-ended and does not exclude additional, unrecited integers or method/process steps.

[0128] “Microcapsules” should be understood to mean generally spherical particles comprising gelled polymer for example denatured protein having an average diameter of 50 to 500 microns as determined using the light microscopy method described below. Preferably the microparticles have an average diameter of 50-200 microns as determined using the light microscopy method described below. Preferably the microparticles have an average diameter of 80-200 microns as determined using the light microscopy method described below. Preferably the microparticles have an average diameter of 80-150 microns as determined using the light microscopy method described below. Depending on the method of manufacture, the microparticles may be microbeads or microcapsules. The microcapsules may have a continuous polymerised matrix and an active agent dispersed throughout the pea protein matrix (i.e. multinuclear). Methods of producing multinuclear microcapsules are described in WO2016/096929. The microcapsules may have a core-shell morphology (i.e. mononuclear—active agent core and protein matrix shell). The core may be a liquid or a solid, or indeed a gas. Methods of producing mononuclear microcapsules are described in WO2014/198787.

[0129] “Meltable coating composition” refers to a composition comprising a wax component and an oil component that that is configured to be solid at ambient (i.e. room) temperature (i.e. at or below 25° C.) and have a melting point temperature that does not damage the matrix or active agent. Generally, the melting point temperature is less than 100° C. although for some protein matrices and active agents higher melting pointing temperatures may be employed. . Preferably, the coating composition has a melting point of 70-100° C., 80-100° C., 90-100° C., 65-100° C., 65-90° C., 70-90° C., 80-90° C., and ideally about 95° C. Typically, the coating composition is prepared my heating the wax and oil component to a melting temperature, and then ideally homogenising the wax and oil to provide the meltable coating composition. Generally, the melting point of the wax is different to the melting point of the oil

[0130] “Wax” refers to one or more natural waxes of plant or animal origin. Generally the wax has not been subjected to secondary chemical treatment such as hydrogenation. Examples of plant waxes include carnauba, berry, myrica fruit, candelilla, tea, rice bran, sunflower wax.

[0131] Examples of animal waxes include beeswax, Chinese, lanolin, shellac, and spermaceti waxes. Preferably, the wax is selected from beeswax and carnauba wax. Preferably the wax comprises a combination of beeswax and carnauba wax. In one embodiment the coating comprising comprises 40-90% wax, 50-80% wax, 55-75% wax, 60-70% wax, and ideally about 66% wax. In one embodiment, the coating comprises beeswax plus an additional wax, for example a plant wax such as carnauba wax. In one embodiment the coating comprising comprises 20-50%, 20-40%, 30-40%, or about 33% beeswax. In one embodiment, the beeswax makes up about 30-70% or 40-60% of the wax component of the coating comprising. In one embodiment, the wax has a melting point above 40° C., 50° C., 60° C., 70° C., 80° C. or 90° C.

[0132] In one embodiment, the coating composition comprises a wax component and an oil component. “Oil” refers to a plant or animal oil or butter, preferably a plant oil or butter. In one embodiment, the oil or butter is solid at room temperature and has a melting point above 20° C., 30° C., 40° C., 50° C., 60° C. or 70° C. Examples of oils or butter include coconut, cocoa, avocado, olive, stearic acid, sunflower, palm or sweet almond butters or derived oils, including chemical treatment such as hydrogenation.

[0133] The microcapsules are generally produced by cold gelation, which means extrusion of microdroplets, and immersion of the microdroplets in a gelation bath configured to cause the protein to polymerise to form a gelled bead. The gelling bath may be an acidic gelling bath.

[0134] “Extrusion” typically means passing the solution/suspension through a small orifice whereby the solution is broken up into micro-size droplets. Preferably, the solution is extruded through an orifice. Various methods will be apparent to the skilled person for generating droplets, for example prilling and spraying (ie spray drying). A preferred method of producing the microdroplets is a vibrating nozzle technique, in which the suspension is sprayed (extruded) through a nozzle and laminar break-up of the sprayed jet is induced by applying a sinusoidal frequency with defined amplitude to the spray from the nozzle.

[0135] Examples of vibrating nozzle machines are the Encapsulator and a machine produced by Nisco Engineering AG. Typically, the spray nozzle has an aperture of between 50 and 600 microns, preferably between 50 and 200 microns, suitably 50-200 microns, typically 50-150 microns, and ideally about 80-150 microns. Suitably, the frequency of operation of the vibrating nozzle is from 900 to 3000 Hz. Generally, the electrostatic potential between nozzle and acidification bath is 0.85 to 1.3 V. Suitably, the amplitude is from 4.7 kV to 7 kV. Typically, the falling distance (from the nozzle to the acidification bath) is less than 50 cm, preferably less than 40 cm, suitably between 20 and 40 cm, preferably between 25 and 35 cm, and ideally about 30 cm. The flow rate of suspension (passing through the nozzle) is typically from 3.0 to 10 ml/min; an ideal flow rate is dependent upon the nozzle size utilized within the process.

[0136] “Acidic gelling bath” means a bath having a pH below the pl of the matrix protein that is capable of instantaneously gelling the droplets. Typically, the acidic gelling bath has a pH of about 4.6. The acidic gelling bath is generally formed from an organic acid. Ideally, the acid is citric acid. Typically, the acidic gelling bath has an acid concentration of 0.1M to 1.0M, preferably 0.3M to 0.7M, and more preferably 0.4M to 0.6M. Typically, the acidic gelling bath has a citric acid concentration of 0.1M to 1.0M, preferably 0.3M to 0.7M, and more preferably 0.4M to 0.6M. Preferably, the acidic gelling bath comprises 0.4 to 0.6M citric acid and has a pH of less than 4.8, typically 4.4 to 4.7.

[0137] “Cured in the acidic gelling bath” means that the microbeads are allowed to remain in the gelling bath for a period of time sufficient to cure (harden) the microbeads. The period of time varies depending on the microbeads, but typically a curing time of at least 30 minutes is employed.

[0138] “Nozzle assembly” means an apparatus comprising at least one nozzle that is configured for extruding the protein solution through the at least one nozzle. In one embodiment, nozzle assembly comprises a single nozzle, whereby a mixture of active agent and protein solution may be extruded the single nozzle to form droplets which when gelled form microbeads. In another embodiment, the nozzle assembly comprises an outer nozzle concentrically arranged around an inner nozzle, and in which the protein solution is extruded through the outer nozzle and an active agent solution/suspension/dispersion is extruded through the inner nozzle to form droplets which when gelled form microencapsulates with a gelled protein shell and an active agent containing core. In another embodiment, the nozzle assembly comprises an outer nozzle concentrically arranged around an inner nozzle, and in which the protein solution and active agent is extruded through the inner nozzle and the coating compositions is extruded through the outer nozzle to form droplets which when gelled form microencapsulates with a gelled active agent containing core surrounded by a shell of coating composition.

[0139] “Active agent” means any component suitable for delivery to the mammalian small intestine or ileum, but typically means a component that is sensitive to an external condition for example heat, pH, pressure, chemical stress or enzymes. Thus, the active component may be sensitive to pH, enzymes (i.e. protease enzymes), high pressure, high shear, and temperature abuse during storage. In one particularly preferred embodiment of the invention, the active component is a cell, typically a bacterial cell, and ideally a probiotic cell. Such cells are sensitive to low pH conditions, such as would be encountered in the stomach, and as such need to be shielded from gastric pH and bile salt environments. Probiotic bacteria, and indeed other types of cells, are also sensitive to high shear or high pressure, such as are employed in conventional methods of generating micron-sized polymer beads. Other types of active components which may be encapsulated in the microbeads of the invention include micronutrients, vitamins, minerals, enzymes, starter bacteria, cell extracts, proteins and polypeptides (native or denatured), sugars and sugar derivatives, nucleic acids and nucleic acid constructs, pharmaceutically-active agents, imaging dyes and ligands, antibodies and antibody fragments, phytochemicals and the like.

[0140] “Active agent solution” means an active agent contained within a suitable liquid carrier in the form of a solution, dispersion or suspension.

[0141] “Drying” as applied to the microcapsules uses powder drying technology such as vacuum drying, fluidised bed drying or spray drying. Generally, the microcapsules are dried to a low moisture level, for example a water activity (a.sub.w) of less than 0.4, 0.3 or 0.2. In one preferred embodiment, the microcapsules are dried using vacuum drying. Powder drying techniques are described in the following: Broeckx, G., Vandenheuvel, D., Claes, I. J., Lebeer, S., & Kiekens, F. (2016). Drying techniques of probiotic bacteria as an important step towards the development of novel pharmabiotics. International Journal of Pharmaceutics, 505(1-2), 303-318; Singh, S., & Dixit, D. (2014). A review on spray drying: Emerging technology in food industry. International Journal of Applied Engineering and Technology, 4(1), 1-8. Emami, F., Vatanara, A., Park, E., & Na, D. (2018). Drying technologies for the stability and bioavailability of biopharmaceuticals. Pharmaceutics, 10(3), 131. Benelli, L., Cortes-Rojas, D. F., Souza, C. R. F., & Oliveira, W. P. (2015). Fluid bed drying and agglomeration of phytopharmaceutical compositions. Powder technology, 273, 145-153.

[0142] “Water activity” (a.sub.w) is the partial vapor pressure of water in a substance divided by the standard state partial vapor pressure of water. It is measured by the method described in Carter, B. P., Galloway, M. T., Campbell, G. S., & Carter, A. H. (2015). The critical water activity from dynamic dewpoint isotherms as an indicator of pre-mix powder stability. Journal of Food Measurement and Characterization, 9(4), 479-486. The operator's manual of the equipment used is provided at http://manuals.decaqon.com/Manuals/13893_AquaLab%20Pre_Web.pdf

[0143] “Coating the microcapsules” refers to the treatment of the microcapsules with the meltable coating composition resulting in the microcapsules being coating with a film of meltable coating composition. Methods of coating include mixing the coating composition with the dried microcapsules in a vessel. The meltable coating composition is heated to melt the coating composition, added to the microcapsules, and agitated until the microcapsules have been coated and the coating has solidified. Alternatively, the microcapsules can be coated with coating composition using a fluidised bed dryer (Teunou, E., & Poncelet, D. (2002). Batch and continuous fluid bed coating—review and state of the art. Journal of food engineering, 53(4), 325-340)). Generally, the coating step employs coating composition and microcapsules in a weight ratio of about 0.5:1.0 to 1.0:5, preferably 0.75:1.0 to 1.0:0.75, and ideally a ratio of about 1:1.

EXEMPLIFICATION

[0144] The invention will now be described with reference to specific Examples. These are merely exemplary and for illustrative purposes only: They are not intended to be limiting in any way to the scope of the monopoly claimed or to the invention described.=These examples constitute the best mode currently contemplated for practicing the invention.

Example 1

Process of Making Coated Micro-Capsules

[0145] A probiotic frozen biomass was homogeneously dispersed in heat denatured protein solution (approximately 9-15% solid content).

[0146] This mixture is extruded throughout a vibrating nozzle (150-450 micron). Polymerisation is induced using an acidification bath comprised by the buffer of a sodium salt of an organic acid (0.1-1 M), and a divalent inorganic salt (0.1-1 M), adjusted to a final pH of 4.0-5.2.

[0147] The resultant wet microcapsules were collected and washed. The microcapsules were dried to moisture content of <4.0% and Aw of 0.2.

[0148] Separately, a coating solution consisting of a mixture of carnauba wax, beeswax and coconut oil (weight ratio 1:1:1) was prepared by heating to 95° C. and homogenised using a high sheer mixer at 10,000 rpm for 60 seconds.

[0149] The subsequent blend was maintained at 70-95° C. until required.

[0150] In a separate container, dry microcapsules and the coating solution were mixed in a ratio of 1:1 and agitated until the coating solution solidified due to a reduction in temperature yielding individual coated microcapsules.

[0151] Microcapsules were collected and sieved for and analysed for moisture content of <4.0% and Aw of 0.2.

Example 2

Process of making Coated Micro-Capsules

[0152] Dried microcapsules were produced according to Example 1.

[0153] Separately a coating solution consisting of a mixture of mixture of carnauba wax and coconut oil (weight ratio 1:1) was prepared by heating to 70-95° C. and homogenised using a high sheer mixer at 10,000 rpm for 60 seconds.

[0154] The subsequent blend was maintained at 95° C. until required.

[0155] In a separate container, dry microcapsules and the coating solution were mixed in a ratio of 1:1 and agitated until the coating solution solidified due to a reduction in temperature yielding individual coated microcapsules.

[0156] Microcapsules were collected and sieved for and analysed for moisture content of <4.0% and Aw of 0.2.

Example 3

Process of Making Coated Micro-Capsules

[0157] Dried microcapsules were produced according to Example 1.

[0158] Separately, a coating solution consisting of a mixture of carnauba wax, beeswax and coconut oil (weight ratio 1:1:1) was prepared by heating to 70-95° C. and homogenised using a high sheer mixer at 10,000 rpm for 60 seconds.

[0159] The subsequent blend was maintained at 95° C. until required.

[0160] Microcapsules were collected and sieved for and analysed for moisture content of <4.0% and Aw of 0.2.

Example 4

Process of Making Coated Micro-Capsules

[0161] Dried microcapsules were produced according to example 1.

[0162] Separately a coating solution consisting of a mixture of carnauba wax, beeswax and coconut oil (weight ratio 1:1:1) was prepared by heating to 70-95° C. and homogenised using a high sheer mixer at 10,000 rpm for 60 seconds.

[0163] The subsequent blend was maintained at 95° C. until required.

[0164] The dried microcapsules were subsequently fluidised using an appropriate apparatus keeping the coating solution at a temperature of 70-150° C.

[0165] The coating solution was sprayed utilising a heated vessel, tubing and nozzle setup (whereby the temperature of the blend was maintained as required) onto the fluidised microcapsules.

[0166] The amount of solution sprayed onto the capsules was between 20-200% of the original weight of the microcapsule powder in the fluidisation chamber.

Example 5

Conducting Stability on Coated Micro-Capsules

[0167] The hydrophobic properties imparted via the coating process were analysed by placing non-coated microcapsules (as described in example 1) and coated microcapsules (as described in example 3) in a high humidity environment (relative humidity 75%) for 120-800 hours).

[0168] Prior to the test, coated microcapsules were standardised in their superficial moisture at 10-15% RH for 24 h. Moisture uptake as a function of weight gain (%) with respect to the initial weight was recorded to demonstrate the hydrophobicity of the coating material. Non-coated microcapsules increased in weight by 10.8 to 11% while coated microcapsules increased in weight by approximately 2 to 6.8%, depending on the formulation.

[0169] The final moisture content (%) after 120-800 h of incubation at 71-75% RH for the control microcapsules and the coated microcapsules, was mathematically calculated from a normalized initial moisture content (%) of 4% w.b. using the weight gain (%) with respect to the initial weight of each formulation.

Example 6

Process of Making Coated Micro-Capsules

[0170] Disperse freezed dried probiotic culture in protein solution (10-15%) and agitate for 20 minutes at room temperature

[0171] Add denatured protein (9%-15% protein content) to the probiotic suspension and agitate.

[0172] Feed this probiotic-protein slurry to the inner core nozzle of a double concentric nozzle extruder

[0173] Feed a solution of prewarmed wax—oil solution to the outer shell nozzle of the double concentric nozzle extruder.

[0174] The ratio of each nozzle diameter can vary depending on the % coating needed

[0175] Maintain both premixes under slight stirring during the process (100 rpm).

[0176] Adjust the pressure to generate a stable bead chain for free fall into the polymerization buffer

[0177] Typically a pressure of 50-800 mBar is adequate for such probiotic—wax—oil suspensions

[0178] Microcapsules are polymerized in a citrate and /or acetate buffer (0.2-0.6M) at temperature between 15-59° C.

[0179] Collect the microcapsules generated and wash in sterile water.

[0180] Dry microcapsules to a moisture content less 4% and Aw less than 0.2.

[0181] The oil+wax coating layer applied can range from 20% to 200% of the original solids content of the feed.

Example 7

Process of Making Coated Micro-Capsules

[0182] Disperse probiotic culture in protein powder and agitate for 20 minutes at room temperature

[0183] Add denatured protein (9%-15% protein content) to the probiotic suspension and agitate.

[0184] Feed this probiotic-protein slurry to the inner core nozzle

[0185] Feed a solution of denatured protein (5%-12% protein content) to the outer shell nozzle.

[0186] The ratio of each nozzle diameter can vary depending on the % coating needed

[0187] Maintain both premixes under slight stirring during the process (100 rpm).

[0188] Adjust the pressure to generate a stable bead chain for free fall into the polymerization buffer

[0189] Typically a pressure of 50-800 mBar is adequate for such probiotic—protein suspensions

[0190] Microcapsules are polymerized in a citrate and/or acetate buffer (0.2.-0.6M) at temperature between 15-50° C.

[0191] Collect the microcapsules generated and wash in sterile water.

[0192] Dry microcapsules to a moisture content less 4% and Aw less than 0.2.

[0193] The protein coating layer applied can range from 20% to 200% of the original solids content of the feed.

Example 8

Process of Making Protected Microparticles

[0194] Disperse freeze dried probiotic culture in a protein powder (with min. calcium content of 1%) powder

[0195] Mix powder for 20 minutes in dry blender

[0196] Fluidise the powder blend for 20 minutes at 40° C. fluidised using an appropriate apparatus

[0197] Coat the fluidised powder with a denature protein solution at a temperature of 20-40° C.

[0198] The coating solution is sprayed using a nozzle diameter from 50-600 um

[0199] The amount of solution sprayed onto the protein and culture is between 10-200% of the original weight of the protein powder

[0200] Collected microparticles and sieve.

[0201] Dry microparticles should have a moisture content less 4% and Aw less than 0.2.

Equivalents

[0202] The foregoing description details presently preferred embodiments of the present invention.

[0203] Numerous modifications and variations in practice thereof are expected to occur to those skilled in the art upon consideration of these descriptions. Those modifications and variations are intended to be encompassed within the claims appended hereto.