Method for manufacturing granules containing plant extract powder

Abstract

To provide a method for efficiently producing a granule that instantly dissolves in water without changing the component composition of a plant extract-derived powdery raw material and without producing joint flour (mamako).SOLUTION: Provided is a method for producing a plant extract powder-containing granule that includes a step of subjecting a plant extract powder raw material to fluidized bed granulation to obtain a granule of plant extract powder, and the method is characterized by (I) performing fluidized bed granulation by spraying water containing no binder as a binding liquid onto the plant extract powder raw material, or (II) performing fluidized bed granulation by using a water-containing powder raw material as a plant extract powder raw material and not spraying a binding liquid.SELECTED DRAWING: Figure 2

Description

[Technical Field]

[0001] The present invention relates to a method for producing granules containing plant extract powder and the resulting granules containing plant extract powder. [Background technology]

[0002] Plant extracts contain health-promoting ingredients and are attracting attention as active ingredients in foods for specified health uses, etc. Technology to granulate plant extract powders is being investigated to make plant extracts easier to take.

[0003] Generally, powder products made from plant extract-derived raw materials have small particle sizes, which makes them prone to clumping when mixed with water, making them difficult to dissolve in water. Clumping occurs when the powder is added to an aqueous solution, and only the surface of the powder aggregates hydrates and dissolves, preventing water from reaching the interior of the aggregates. This clumping, also known as lumps, occurs when the powder is added to an aqueous solution and only the surface of the aggregates hydrates and dissolves, preventing water from reaching the interior of the aggregates. When clumps occur, the powder is difficult to dissolve in water, and in order to achieve complete dissolution, it is necessary to increase the stirring intensity or prolong the stirring time.

[0004] Conventionally, plant extract granules have been produced by compressing and integrating powder raw materials with a binder, and fluidized bed granulation equipment is generally used to produce dry granules. The granulation mechanism by fluidized bed granulation involves keeping the base powder in a fluidized bed, spraying a binder-containing liquid into the bed, and agglomerating the powder with the binder, which then dries and granulates it.

[0005] For example, Patent Document 1 discloses a method for granulating a powder of a plant-derived polyphenol-containing extract by fluidized bed granulation, in which a binder such as hydroxypropyl cellulose is used in the granulation process.

[0006] As described above, it has been common to use a binder in fluidized bed granulation, but this has the drawback of making the resulting granules less soluble in water and changing the ingredients and composition of the final product. [Prior art documents] [Patent documents]

[0007] [Patent Document 1] Japanese Patent Application Laid-Open No. 2010-154769 Summary of the Invention [Problem to be solved by the invention]

[0008] An object of the present invention is to provide a method for efficiently producing granules that dissolve instantly in water without changing the component composition of a powdered raw material derived from a plant extract and without forming lumps. [Means for solving the problem]

[0009] As a result of intensive research by the inventors to solve the above problems, they discovered that when performing fluidized bed granulation, water that does not contain a binder (binding promoter) is sprayed onto the plant extract powder raw material as the spray liquid (binding liquid) and fluidized bed granulation is performed, or by using a powder raw material that contains water as the plant extract powder raw material and performing fluidized bed granulation without spraying a binding liquid, it is possible to efficiently form granules of plant extract powder, and the resulting granules are instantly soluble granules that dissolve instantly in water without forming lumps, which led to the completion of the present invention.

[0010] That is, the present invention includes the following. [1] A method for producing plant extract powder-containing granules, comprising a step of subjecting a plant extract powder raw material to fluidized bed granulation to obtain plant extract powder granules, (I) Spraying binder-free water as a binding liquid onto the plant extract powder raw material and performing fluidized bed granulation; or (II) Using a powdered raw material containing moisture as the plant extract powdered raw material, and performing fluidized bed granulation without spraying a binding liquid, A method characterized by: [2] The method according to [1], wherein in (I), the total amount of water contained in the plant extract powder raw material and the sprayed water is 2.5% by weight or more and 30% by weight or less of the total amount of the plant extract powder raw material. [3] The method according to [1], wherein in (II), the amount of water contained in the powdered plant extract raw material is 2.5% by weight or more and 10% by weight or less, based on the total amount of the powdered plant extract raw material. [4] The method according to any one of [1] to [3], wherein the plant extract is bilberry extract or apple extract. [5] Granules containing plant extract powder obtained by the method described in any one of [1] to [4]. [6] A food product comprising the plant extract powder-containing granules described in [5]. [Effects of the Invention]

[0011] According to the present invention, it is possible to efficiently obtain granules of plant extract powder that instantly dissolve in water without forming lumps. By spraying binder-free water as a binding liquid onto the plant extract powder raw material and performing fluidized bed granulation, or by using a water-containing powder raw material as the plant extract powder raw material and performing fluidized bed granulation without spraying a binding liquid, not only can the manufacturing process be simplified, but granules can be obtained without changing the component composition of the plant extract-derived powder raw material, facilitating commercialization. [Brief explanation of the drawings]

[0012] [Figure 1] FIG. 1 shows the results of analyzing the particle size composition of granules obtained when fluidized bed granulation was performed while changing the amount of water spray. [Figure 2] FIG. 1 shows the results of analyzing the bulk density of granules obtained when fluidized bed granulation was performed while changing the amount of water sprayed. DETAILED DESCRIPTION OF THE INVENTION

[0013] <Method of manufacturing granules containing plant extract powder> The present invention relates to a method for producing granules containing plant extract powder, which includes a step of subjecting a plant extract powder raw material to fluidized bed granulation to obtain plant extract powder granules, and is characterized by (I) spraying binder-free water as a binding liquid onto the plant extract powder raw material and performing fluidized bed granulation, or (II) using a powder raw material containing water as the plant extract powder raw material and performing fluidized bed granulation without spraying a binding liquid.

[0014] <Plant extract powder> The plant extract powder used as the raw material can be obtained, for example, by extracting a fraction containing health-promoting components such as polyphenols from a plant containing the health-promoting components, drying the fraction, and powdering it. The plant extract powder may contain multiple health-promoting components, or may contain components other than the health-promoting components. Commercially available plant extract powders may be used. The type of health-promoting component is not particularly limited, but examples include polyphenols, anthocyanins, anthocyanidins, naringin, silibinin, isoflavones, steviol, glycyrrhizin, ellagic acid, citric acid, chlorogenic acid, malic acid, and the like.

[0015] The extraction method for plant extracts is not particularly limited, and an appropriate method may be selected depending on the type, part, and type of health-promoting component of the plant, and any method commonly used by those skilled in the art may be used. For example, plants may be extracted by solvent suspension, drying, mechanical crushing, squeezing, supercritical extraction, or other procedures. These extraction procedures may be performed alone or in combination. Solvents used for extraction include water and organic solvents such as chloroform, hexane, acetone, methanol, and ethanol, and can be selected appropriately depending on the type of health-promoting component. Drying may be performed using conventional methods such as tray drying, fluidized bed drying, flash drying, and spray drying. Mechanical pulverization may be performed using either a wet or dry method, such as a bead mill, roll mill, hammer mill, jet mill, or pin mill. Compression may be performed using conventional methods.

[0016] The type of plant is not particularly limited as long as it contains the above-mentioned health-promoting components. Examples of the plant include berries, apples, Drynaria fortunei, milk thistle (Silybum marianum), soybeans, stevia, and licorice are examples. The plant extract may be any extract containing the health-promoting components described above, but preferably contains carbohydrates, and more preferably contains 80% by weight or more of carbohydrates. Examples of plant extracts include berry extracts (aronia extract, elderberry extract, cranberry extract, black bean extract, cowberry extract, strawberry extract, bilberry extract, blackcurrant extract, blackberry extract, blueberry extract, boysenberry extract, raspberry extract, lingonberry extract, redcurrant extract), apple extract, bone extract, milk thistle extract, soybean extract, stevia extract, licorice extract, etc.

[0017] There are no particular limitations on the powder as long as it has a particle size that can be subjected to fluidized bed granulation, and it can be selected appropriately depending on the type of raw material. The powder to be subjected to fluidized bed granulation may contain moisture, and if it contains moisture of 2.5% by weight or more, preferably 2.8% by weight or more, it can also be used in the granulation method (II) of the present invention described below.

[0018] <Fluidized bed granulation> Fluidized bed granulation can be carried out by known methods. The plant extract powder raw material is placed in a fluidized bed granulator or similar granulation device, and water is sprayed onto the plant extract powder raw material and stirred under a hot air current. For example, hot air is blown into the lower part of the granulation chamber of the fluidized bed granulation device, and the raw plant extract powder is lifted into the air to form a layer in which the particles are fluidized. Then, a granulation liquid (water) is sprayed onto the raw plant extract powder, causing the particles to aggregate and grow into granules. Note that if the plant extract powder raw material contains a certain amount of water or more, granulation can be achieved simply by fluidizing the plant extract powder raw material using the water contained in the raw plant extract powder without spraying water.

[0019] In the embodiment (I) of the method of the present invention, water containing no binder is sprayed as a binding liquid onto the plant extract powder raw material to carry out fluidized bed granulation. Here, the binder is a substance that promotes granulation, and examples thereof include hydroxypropyl cellulose, hydroxypropyl methyl cellulose, sodium carboxymethyl cellulose, polyvinylpyrrolidone, etc. In the method of the present invention, water alone may be used as the granulation liquid, but the water may also contain water-soluble components other than the binder. In the method of embodiment (I) of the present invention, it is preferable to set the amount of water used in fluidized bed granulation within a certain range. Specifically, it is preferable to adjust the total amount of water contained in the plant extract powder raw material and the sprayed water to be 2.5% by weight or more and 30% by weight or less of the total amount of the plant extract powder raw material. In other words, when granulating the prepared plant extract powder raw material, it is preferable that the total amount of water not including the binder sprayed as the granulation liquid and the amount of water contained in the plant extract powder raw material before the granulation is completed be 2.5% by weight or more and 30% by weight or less of the total amount of the plant extract powder raw material. The lower limit is more preferably 2.8% by weight or more, The upper limit is more preferably 25% by weight or less.

[0020] In the embodiment (II) of the method of the present invention, a powdery raw material containing moisture is used as the plant extract powdery raw material, and fluidized bed granulation is carried out without spraying a binding liquid. Here, the water content contained in the plant extract powder raw material is preferably 2.5% by weight or more, and more preferably 2.8% by weight or more. The upper limit of the water content may be such that the plant extract powder raw material can be fluidized within the fluidized bed, for example, 10% by weight or less, or 6% by weight or less.

[0021] The temperature inside the granulation chamber during granulation can be, for example, 30°C to 50°C.

[0022] <Granules> The granules obtained by the method of the present invention are instantly soluble. Here, "instantly soluble" means that when the granules are dropped onto the surface of water, they immediately settle and dissolve without forming a powder, for example, within 30 seconds. The granules obtained by the method of the present invention preferably have a bulk density of 0.45 g / ml or less. There is no particular lower limit, but it is preferably, for example, 0.10 g / ml or more.

[0023] The granules obtained by the method of the present invention may be taken as they are, or may be taken as a preparation in which the granules are encapsulated in a capsule or the like. The capsule may be a hard capsule or a soft capsule. The preparation containing the granules obtained by the method of the present invention may contain other optional ingredients such as sweeteners, flavorings, excipients, coloring agents, etc., as long as they do not interfere with the effects of the health-promoting ingredients or the immediate solubility of the granules.

[0024] <Food> The granules obtained by the method of the present invention or a preparation containing the same can be used as a food product. Since the granules do not contain a binder, the binder is not included in the food product when the granules are made into the food product, and therefore the plant extract can be used as is without changing its components. The food may be a functional food. Functional foods refer to foods that have superior physiological properties compared to ordinary foods, such as health foods, health supplements, foods for patients, nutritional supplements, or foods with health claims defined by the Ministry of Health, Labor and Welfare (foods for specified health uses, foods with nutrient functions, and foods with functional claims). The composition of the present invention can be used as an ingredient in health foods, health supplements, foods for patients, nutritional supplements, foods for specified health uses, foods with nutrient functions, and foods with functional claims. [Example]

[0025] The present invention will be described in more detail below based on examples, but the present invention is not limited to these examples.

[0026] Example 1 As the plant extract powder raw material, bilberry extract powder (MyrtiPRO bilberry extract powder 25.5%, BGG Japan Co., Ltd.) shown in Table 1 was used.

[0027] [Table 1]

[0028] Fluidized bed granulation was carried out using a fluidized bed granulator (FLO-5 model, Freund Corporation) under the conditions shown in Table 2. Granulation was carried out under conditions where the amount of sprayed water was varied to 0%, 21%, 32%, and 43%, and the granulation reaction was continued until the sprayed water was depleted. Since the raw material bilberry extract powder contains 3.2% water, the total amount of water used in granulation is as follows: Spray water amount 0%...3.2% Spray water amount 21%...24.9% Spray water amount 32%...35.7% Spray water amount 43%...46.5%

[0029] [Table 2]

[0030] <Example 2> As the plant extract powder raw material, apple polyphenol powder (ApplePhenon SH, BGG Japan Co., Ltd.), which is an apple extract powder listed in Table 3, was used.

[0031] [Table 3]

[0032] Fluidized bed granulation was carried out using a fluidized bed granulator (Freund Corporation, FLO-5 model) under the conditions shown in Table 4. Granulation was carried out under different conditions, with the amount of water sprayed being 10%, 20%, 30%, and 37%, and the granulation reaction was continued until the sprayed water was depleted. Since the raw material apple polyphenol powder contains 2.9% water, the total amount of water used in granulation was as follows: Spray water amount 10%...12.9% Spray water amount 20%...22.9% Spray water amount 30%...32.9% Spray water amount 37%...39.6%

[0033] [Table 4]

[0034] <Evaluation of granulated products> The granules obtained in Examples 1 and 2 were measured for solubility, particle size, and bulk density.

[0035] The solubility test was carried out by dropping 0.1 g (or 1 g) of the sample on a spoon onto the surface of a 275 ml cup containing 200 ml of water, and visually evaluating the solubility.

[0036] The bulk density was measured as follows. Place a 100 mL stainless steel container for measuring specific gravity on the balance and set the tare to "0.00". Place a stainless steel cylinder upright in the container and pour the sample in the plastic bag into the cylinder from about 5 cm above the top until it overflows. Pull out the stainless steel tube in one go, taking care not to hit the stainless steel container, and scrape off the sample above the top of the stainless steel container without applying any impact. -Weight the sample and calculate the bulk density (g / mL) of the sample using the following formula. Bulk specific gravity (g / mL) = sample weight (g) ÷ 100 mL

[0037] <Result> The evaluation results of the bilberry extract powder granules are shown in Table 5. With powder raw materials that were not granulated, splinting occurred on the water surface and the granules remained on the water surface for more than one minute, but with the granules obtained by fluidized bed granulation with water spray amounts of 0% (total moisture content 3.2%) and 21% (total moisture content 24.9%), the properties were improved to the point that splinting did not occur and the granules immediately settled and dissolved. The properties of the granules obtained by fluidized bed granulation with a mist volume of 32% (total moisture content 35.7%) also changed, and although they settled without forming clumps, the granules remained in the water for more than 1 minute. It was not possible to produce a film with a water spray amount of 43% or more (total water content 46.5%) due to the occurrence of blocking. In this way, it was found that when granulating bilberry extract powder, fluidized bed granulation is possible without spraying water by using powder raw materials containing moisture, and when the total amount of moisture contained in the plant extract powder raw materials and the water sprayed is 3.2 to 24.9 wt% of the total amount of plant extract powder raw materials, it was possible to obtain instantly dissolving granules that immediately settle and dissolve without the occurrence of powder spattering.

[0038] [Table 5] ○, Instant dissolution (immediate settling and dissolution without powder splicing) △: Slow dissolution (settling without powder formation, but granules remain in water for more than 1 minute) ×: Remaining (granules remain on the water surface for more than 1 minute due to powder spattering)

[0039] The evaluation results of the apple polyphenol powder granules are shown in Table 6. With ungranulated powdered raw materials, clumping occurred on the water surface, and the granules remained on the surface for over a minute, but with granules obtained by fluidized bed granulation with a water spray rate of 10% (total moisture content: 12.9%) and 20% (total moisture content: 22.9%), the properties were improved, with the granules settling and dissolving immediately without clumping. Granules obtained by fluidized bed granulation with a water spray rate of 30% (total moisture content: 32.9%) also showed a change in properties, settling without clumping, but remaining in the water for over a minute. It was not possible to produce a film with a water spray amount of 37% or more (total water content 39.6%) due to the occurrence of blocking. Thus, in the granulation of apple polyphenol powder, when the combined amount of water contained in the plant extract powder raw material and the sprayed water was 12.9 to 22.9% by weight of the total amount of plant extract powder raw material, it was possible to obtain instantly dissolving granules that immediately settled and dissolved without any spattering.

[0040] [Table 6] ○, Instant dissolution (immediate settling and dissolution without powder splicing) △: Slow dissolution (settling without powder formation, but granules remain in water for more than 1 minute) ×: Remaining (granules remain on the water surface for more than 1 minute due to powder spattering)

[0041] The results of analyzing the particle size composition of each granule are shown in Figure 1. As a result, the apple polyphenol powder raw material (far left) contains particles so small that they adhere to the sieve with static electricity, but in the granulated product with a water spray volume of 10% or more, there was no "unrecovered" particle size composition.

[0042] The bulk density of the granulated material was also measured to examine the relationship between the amount of sprayed liquid and the bulk density. The results are shown in Figure 2. The bulk density of the bilberry extract powder granules and apple polyphenol powder granules decreased as the amount of water sprayed increased, and a correlation was observed between bulk density and particle size distribution.

Claims

[Claim 1] A method for producing plant extract powder-containing granules, comprising a step of subjecting a plant extract powder raw material to fluidized bed granulation to obtain plant extract powder granules, (I) As a binding liquid, water containing no binder, which is a binding promoter, is used to mix the plant extract powder raw material. spraying the mixture into the container and carrying out fluidized bed granulation; In (I), the total amount of water contained in the plant extract powder raw material and the water to be sprayed is The content of the extract powder raw material is 2.5% by weight or more and 30% by weight or less relative to the total amount of the extract powder raw material; and The plant extract is bilberry extract or apple extract. A method characterized by:

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