WO2023286707A1 - 造粒物及びその製造方法 - Google Patents
造粒物及びその製造方法 Download PDFInfo
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- WO2023286707A1 WO2023286707A1 PCT/JP2022/027092 JP2022027092W WO2023286707A1 WO 2023286707 A1 WO2023286707 A1 WO 2023286707A1 JP 2022027092 W JP2022027092 W JP 2022027092W WO 2023286707 A1 WO2023286707 A1 WO 2023286707A1
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
- A23L5/30—Physical treatment, e.g. electrical or magnetic means, wave energy or irradiation
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/01—Instant products; Powders; Flakes; Granules
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/38—Other non-alcoholic beverages
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/385—Concentrates of non-alcoholic beverages
- A23L2/39—Dry compositions
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/198—Dry unshaped finely divided cereal products, not provided for in groups A23L7/117 - A23L7/196 and A23L29/00, e.g. meal, flour, powder, dried cereal creams or extracts
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2300/00—Processes
- A23V2300/10—Drying, dehydrating
Definitions
- the present invention relates to a granulated product containing dry powder of at least one kind of green leaf selected from barley, kale, sweet potato, mulberry, Angelica keiskei, mugwort, Choumeisou, and Kumazasa, and a method for producing the same.
- the green leaves of wheat, kale, sweet potato, mulberry, Angelica keiskei, mugwort, chomeisou and kumazasa (these plants are abbreviated as “green juice ingredients” below) contain nutrients such as vitamins, minerals, and dietary fiber. It contains abundantly and is used as a raw material for so-called green juice. These green leaves are known to have various physiological activities.
- Patent Document 1 describes that a mugwort extract has an anti-obesity effect.
- the green leaves of the above plants are generally used as aojiru after being processed into powder or juice.
- Aojiru is mostly in the form of processed foods (powder beverages) that are mixed with liquids such as water, hot water, milk, and soy milk for drinking, and is widely distributed as powdered beverages.
- the green juice is in the form of a powdered drink
- the task of dispersing the powdered drink in a liquid such as water is the responsibility of the consumer at the time of ingestion.
- a green juice that has excellent dispersibility (easily dispersed in liquid, etc.) and is easy to drink (less mushy).
- the present invention has been made in view of the above problems, and contains dry powder of at least one green leaf selected from wheat, kale, sweet potato, mulberry, Angelica keiskei, mugwort, long-life grass and kumazasa.
- the object of the present invention is to provide a granule which is excellent in dispersibility and ease of drinking, and a method for producing the same.
- the present inventors obtained granules excellent in dispersibility and ease of drinking by controlling the specific gravity of the granules within a certain range and controlling the particle size distribution within a certain range. The present inventors have found that it is possible to achieve the present invention.
- the present invention is as follows.
- a method for producing a granule containing dry powder of at least one kind of green leaf selected from barley, kale, sweet potato, mulberry, angelica keiskei, mugwort, chomeisou and kumazasa A raw material containing dry powder of green leaves is put into a fluidized bed granulator, air is supplied to fluidize the raw material, water is sprayed, and then dried to obtain granules, A method for producing granules, wherein the granules have a specific gravity of less than 0.300 g/cm 3 .
- a granule is produced using a dry powder of at least one green leaf selected from barley, kale, sweet potato, mulberry, Angelica keiskei, mugwort, long-life grass, and kumazasa, and the granule is Granules with excellent dispersibility and ease of drinking can be provided by controlling the specific gravity of the liquid within a certain range.
- the green juice material in the present invention means at least one kind of plant selected from barley, kale, sweet potato, mulberry, Angelica keiskei, mugwort, Chomeisou and Kumazasa. Only one kind may be used, or two or more kinds may be used.
- the green leaves of the aojiru ingredient in the present invention mean a plant body containing the leaf portion of the aojiru ingredient, and may include the stem and other parts as well as the leaves. At the time of harvesting, it takes labor to remove the stem from the ground and sort out only the leaf part, and the stem part also contains abundant nutritional components such as insoluble dietary fiber, so from the viewpoint of reducing production costs and nutritional benefits. Therefore, it is preferable to include stems as well as leaves.
- the barley in the present invention is a general term for plants of the Gramineae family with similar appearances, such as barley, wheat, rye, and oats. Barley is particularly preferred as the barley in the present invention.
- Barley (Hordeum vulgare L.) is considered to be native to Central Asia and is an annual or perennial herb belonging to the Poaceae family.
- the variety of barley used in the present invention is not particularly limited. Any variety of barley can be used, and wild varieties and hybrids can also be used. Examples thereof include two-rowed barley, six-rowed barley, and naked barley, and these can be used singly or in combination of two or more.
- the green leaves of barley may be those harvested at any harvest time, and are not particularly limited. It is preferable to use the one (barley young leaves) harvested in the early days. Specifically, for example, it is preferable to use young barley leaves harvested from barley with a height of 10 cm or more, preferably about 10 to 90 cm, particularly preferably about 20 to 80 cm, particularly about 30 to 70 cm.
- Kale in the present invention belongs to the genus Brassica of the Brassicaceae family, and the scientific name is Brassica oleracea var. means a plant that is acephala.
- the variety of kale is not particularly limited, and various kinds of kale such as kitchen kale, tree kale, bush kale, mallow kale, collard greens, and green leaf kale can be used.
- the green leaves of kale may be those harvested at any harvest time, and are not particularly limited.
- the sweet potato in the present invention means a plant belonging to the genus Ipomoea of the Convolvulaceae family and whose scientific name is Ipomoea batatas.
- the sweet potato is not particularly limited as long as it is generally called sweet potato.
- the variety of sweet potato is not particularly limited, and examples thereof include varieties such as Suio, Joy White, Kogane Sengan, Shiroyutaka, Satsuma Mustachi, and Ayamurasaki. Among them, watermelon with a high polyphenol content is preferable.
- the green leaves of the sweet potato may be those harvested at any harvest time, and are not particularly limited. Stems and leaves are more preferred.
- Mulberry in the present invention means a plant belonging to the genus Morus of the family Moraceae.
- the species of mulberry is not particularly limited, and mulberry, yamaguwa, logwa, long mulberry, kegwa, ogasawara gua, tenjikuwa and the like can be used.
- Mulberry green leaves may be harvested at any harvest time, and are not particularly limited.
- Angelica keiskei in the present invention means a plant belonging to the genus Angelica of the family Umbelliferae and having the scientific name Angelica keiskei.
- the variety of Angelica keiskei is not particularly limited and can be used as appropriate.
- the green leaves of Angelica keiskei may be those harvested at any harvest time, and are not particularly limited.
- Mugwort in the present invention means a perennial plant belonging to the genus Artemisia of the Asteraceae family.
- the species of mugwort is not particularly limited, but mugwort, wormwood absinthium, tarragon, wormwood nitro, wormwood onio, wormwood wormwood, wormwood, wormwood, wormwood, carrot, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood takane , wormwood, wormwood, white wormwood, wormwood, wormwood, wormwood, cotton wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood, wormwood,
- Chomeisou in the present invention means a plant belonging to the genus Kawarabofu of the family Umbelliferae and whose scientific name is Peucedanum japonicum.
- Chomeisou is called Botanbofu, Choumeisou, Chomeigusa, Chomifusa, Bohu, Sakuna, Upubasafuna, Chomigusa, Botanfufu, etc. depending on the region.
- the variety of Chomeisou is not particularly limited and can be used as appropriate.
- the green leaves of Chomeisou are not particularly limited and may be those harvested at any harvest time.
- Kumazasa in the present invention means a plant belonging to the genus Sasa of the family Poaceae.
- the species of Kumazasa is not particularly limited, and Sasa veitchii, Sasa kurilensis, Sasamorpha borealis, Sasa senanensis, Sasa palmata, Sasa niponica, etc. can be used.
- the green leaves of Kumazasa may be harvested at any harvest time, and are not particularly limited.
- the dry powder of green leaves in the present invention means a product obtained by processing at least one kind of green leaves selected from barley, kale, sweet potato, mulberry, Angelica keiskei, mugwort, Chomeisou and Kumazasa into dry powder.
- Examples of the dry powder of green leaves include those obtained by pulverizing green leaves into dry powder (pulverized green leaves), dry powders of squeezed green leaves (powder of squeezed green leaves), and dried green leaf extracts. Examples include, but are not limited to, powdered products (green leaf extract powder).
- the dry powder of green leaves of the present invention is preferably pulverized powder of green leaves from the viewpoints of excellent dispersibility and ease of drinking, ease of processing, storage, transportation, etc., and rich dietary fiber. preferable.
- the pulverized powder of green leaves in the present invention for example, one obtained by combining drying treatment and pulverizing treatment can be used.
- the drying treatment and the pulverizing treatment may be carried out simultaneously, or either one may be carried out first, but it is preferable to carry out the pulverizing treatment after the drying treatment.
- one or a combination of two or more treatments selected from treatments such as blanching treatment and sterilization treatment may be performed.
- the number of times of pulverizing treatment is not particularly limited, and the treatment may be performed once or twice or more, such as performing coarse pulverizing treatment followed by fine pulverizing treatment for more finely pulverizing.
- the blanching treatment is a treatment to keep the green leaves of the green juice material bright green, and methods of blanching treatment include hot water treatment and steaming treatment.
- the green leaves of the green juice material are preferably soaked in hot water or steam at a temperature of preferably 70 to 100° C., more preferably 80 to 100° C., for preferably 60 to 240 seconds, more preferably 90 to 180° C.
- a method of processing in seconds, etc. can be mentioned.
- the steaming process is preferably an intermittent steaming process in which the green leaves of the aojiru material are repeatedly steamed and cooled under normal or pressurized pressure.
- the steaming treatment is preferably performed for 20 to 40 seconds, more preferably 30 seconds, for example.
- the cooling treatment after the steaming treatment is preferably performed immediately, and the method is not particularly limited, but immersion in cold water, refrigeration, cooling with cold air, evaporative cooling with hot air, and evaporative cooling with a combination of hot and cold air. etc. are used. Among these, evaporative cooling in which warm air and cold air are combined is preferable.
- Such a cooling treatment is performed so that the product temperature of the green leaves of the green juice material is preferably 60° C.
- the sterilization treatment is not particularly limited as long as it is a sterilization treatment commonly known to those skilled in the art.
- it is a treatment that physically or chemically kills microorganisms using temperature, pressure, electromagnetic waves, chemicals, etc. can be done.
- the blanching treatment is preferably performed before the drying treatment.
- the sterilization treatment is preferably performed after the drying treatment or before or after the pulverization treatment.
- the drying process is not particularly limited, for example, a process of drying so that the water content of the green leaves of the green juice material is 10% by weight or less, preferably 5% by weight or less.
- the drying treatment can be performed by any method known to those skilled in the art, such as hot air drying, high-pressure steam drying, electromagnetic wave drying, and freeze drying. Drying by heating can be carried out, for example, preferably at 40° C. to 140° C., more preferably at 80 to 130° C., at a temperature and time at which the green leaves of the green juice material do not discolor.
- the crushing treatment is not particularly limited, but includes, for example, a treatment of crushing the plant by any method commonly used by those skilled in the art.
- a treatment of crushing the plant by any method commonly used by those skilled in the art it is preferable to perform coarse pulverization and fine pulverization in combination from the viewpoint of increasing pulverization efficiency such as homogenization of particle size and reduction of pulverization time.
- the green leaves are cut using any coarse pulverization device or instrument commonly used by those skilled in the art, such as cutters, slicers, and dicers. .Crush to 1-10 mm.
- the fine pulverization step for example, the green leaves of the green juice material are finely pulverized using any fine powder-adopting equipment or equipment commonly used by those skilled in the art, such as crushers, mills, blenders, and millstones. Physical properties such as the specific gravity and particle size distribution of the green leaves of the aojiru material can be adjusted by appropriately setting the conditions for the pulverization treatment based on methods commonly used by those skilled in the art.
- the green leaf juice powder in the present invention for example, one obtained by low-temperature concentrating the green leaf juice to concentrate the solid content and freeze-drying or spray-drying the concentrate can be used.
- the particle size of the dry green leaf powder used as the raw material for the granules in the present invention is not particularly limited, and a raw material having a particle size that facilitates granulation may be appropriately selected and used.
- the particle size of the dry powder of green leaves may be, for example, a median diameter of 60 ⁇ m or less, 50 ⁇ m or less, 40 ⁇ m or less, or 30 ⁇ m or less. 25 ⁇ m or less may be used.
- the median diameter of the dry powder of green leaves is also called D50 or d50, and when the powder is divided into two from the particle size, it refers to the diameter at which the large particle size and the small particle size are equal. It can be measured using a diffraction/scattering method. Specifically, for example, the cumulative 50% ( ⁇ 50) particle size of the particle size distribution measured using LMS-300 or LMS-350 manufactured by Seishin Enterprise Co., Ltd., which is a laser diffraction scattering light particle size distribution measuring device is.
- Granulation means an operation of aggregating a plurality of particles to form aggregates.
- voids are formed between particles when the particles aggregate, and there is a structural difference between the granules and the raw material particles used for granulation.
- the granules containing the green leaf dry powder of the green juice material are granulated using the green leaf dry powder of the green juice material as a raw material, and have a specific gravity of less than 0.300 g/cm 3 . do.
- the granules may further contain raw materials other than the green leaf dry powder of green juice ingredients, such as excipients and sweeteners. By controlling the specific gravity of the granules to fall within the above range, granules with excellent dispersibility and ease of drinking can be obtained.
- the granules of the present invention may be aggregates in which a plurality of particles are aggregated by some method, and the size of the granules is not particularly limited.
- the granulation method in the present invention is not particularly limited, and may be appropriately selected from a granulation method normally used by those skilled in the art.
- a fluid bed granulation method, an extrusion granulation method, a tumbling granulation method, an agitation granulation method, and the like can be mentioned.
- any granulation method any granulation device available on the market is used, and granules satisfying the conditions of specific gravity specified in the present invention are obtained by appropriately setting various manufacturing conditions such as drying temperature. can be manufactured.
- pulverization and classification may be performed to adjust the specific gravity and particle size distribution of the granules.
- the granules of the present invention can be obtained by any granulation method, but fluid bed granulation is particularly preferable from the viewpoint of ease of granulation.
- Fluidized bed granulation involves blowing air onto the raw material powder particles to make them fluidized by the air flow, while spraying a binding liquid such as water to bind the powder particles together. This is a method of forming granules, which are aggregates.
- the dried powder of the green leaves of green juice which is the raw material
- a fluidized bed granulator In the case of fluidized bed granulation, the dried powder of the green leaves of green juice, which is the raw material, is put into a fluidized bed granulator, and air is supplied to fluidize the raw material. Water is sprayed on the raw material, and then it is dried.
- the granules of the present invention can be obtained by a production method comprising the step of obtaining granules.
- a fluidized bed granulator used for granulation any granulator available on the market can be used.
- Granules satisfying the conditions of the present invention can be produced by appropriately setting various production conditions for the granulator according to the properties of the raw material used. Further, the specific gravity and particle size of the granules may be adjusted by classifying or pulverizing the granules obtained as necessary.
- the temperature of the air supplied when fluidizing the raw material there are no particular restrictions on the temperature of the air supplied when fluidizing the raw material, and it may be adjusted as appropriate according to the properties of the raw material used.
- the temperature of the supplied air should be adjusted according to the characteristics of the raw material used. It can be adjusted as appropriate. When the temperature of the supplied air is low, less water evaporates and the powder particles are more likely to get wet.
- the temperature of the air supplied when fluidizing the raw material matches the specific gravity range in the present invention, and the granules are particularly excellent in dispersibility and ease of drinking. 50 to 75°C is preferred, 50 to 70°C is more preferred, and 50 to 60°C is particularly preferred, from the viewpoint that it is easy to obtain
- the temperature of air to be supplied can be set. For example, when it is desired to supply air at 50°C, the set temperature of the fluidized bed granulator should be 50°C.
- the method of spraying water may be either continuous spraying or intermittent spraying.
- Continuous spraying refers to a spraying method in which water spraying is continued without stopping until the entire amount of water is sprayed from the start of water spraying.
- Intermittent spraying refers to a spraying method in which water spraying is stopped at least once between the start of water spraying and the completion of spraying of the entire amount of water. From the viewpoint of obtaining granules particularly excellent in dispersibility and ease of drinking, it is preferable to proceed while adjusting the state of hydration using an intermittent spray technique.
- the concept of spraying water is not limited to spraying only water, but also includes spraying an aqueous solution in which a binder or the like is dissolved in water.
- the amount of water to be sprayed is not particularly limited, and may be appropriately adjusted according to the characteristics of the raw material used.
- the lower limit of the amount of water to be sprayed is 20% by weight or more with respect to the total weight of the raw materials, from the viewpoint that it is easy to obtain granules that are particularly excellent in dispersibility and ease of drinking. It is preferably 30% by weight or more, further preferably 40% by weight or more, particularly preferably 45% by weight or more, and most preferably 50% by weight or more.
- the upper limit of the amount of water to be sprayed is preferably 300% by weight or less, and 250% by weight or less, relative to the total weight of the raw materials from the viewpoint of shortening the drying time and improving productivity.
- the amount of water to be sprayed is the amount with respect to the total weight including raw materials other than the dry powder of the green leaves of the green juice material.
- the granulation process may be performed only once or multiple times.
- the granules of the present invention are excellent in dispersibility and ease of drinking regardless of whether the granulation process is performed once or multiple times. From the viewpoint of productivity, it is more preferable to perform the granulation step once.
- fluidized bed granulation there is a process (drying process) of drying to obtain granules after performing a process of spraying water on the fluidized raw material.
- the temperature of the air supplied during drying is not particularly limited, and may be appropriately adjusted according to the characteristics of the raw material used. From the viewpoints of facilitating the production of granules and shortening the drying time, the temperature is preferably 80° C. or higher, more preferably 90° C. or higher, even more preferably 100° C. or higher, and particularly preferably 110° C. or higher. Since the temperature of the air supplied to the fluidized bed granulator can be set, for example, when it is desired to supply air at 90°C, the set temperature of the fluidized bed granulator should be 90°C.
- the water content of the resulting granules is not particularly limited, but is preferably 10% by weight or less, more preferably 8% by weight or less, even more preferably 7% by weight or less, particularly preferably 6% by weight or less, and 5% by weight. Most preferred are:
- the granules of the present invention may optionally contain additives such as binders, excipients, thickeners, etc., in addition to the dry powder of the green leaves of the green juice material.
- additives are not particularly limited, and examples include sugars such as glucose, maltitol, and erythritol, polysaccharide thickeners such as guar gum, starches such as cornstarch, starch decomposition products such as dextrin and indigestible dextrin, and the like. can be mentioned.
- An additive may add only 1 type and may add 2 or more types.
- the granules of the present invention may be appropriately added with green leaf dry powder of plants other than green juice material.
- green leaves of plants that are not green juice ingredients include green tea leaves, spinach leaves, turnip leaves, and Komatsuna leaves.
- the content of the dry green leaf powder of a plant that is not a green juice material is not particularly limited, but from the viewpoint of dispersibility, ease of drinking or nutritional supplementation, it is more green than the dry green leaf powder of a plant that is not a green juice material. It is preferable that the content (total weight) of the green leaf dry powder in the soup material is large.
- the content of the green leaf dry powder of the green juice material in the granules of the present invention is not particularly limited.
- a powder containing a high content of dry powder of green leaves (especially pulverized powder of green leaves) as a raw material for green juice dispersibility is poor even if granulated, so it is packed as it is without granulation and used as green juice.
- the content of green leaf dry powder of green juice material in the granulated product is preferably 50% by weight or more, more preferably 60% by weight or more, and further preferably 70% by weight or more.
- the green leaf dry powder of the green juice material has the highest content among the raw materials blended in the granules.
- the barley green leaf dry powder is particularly excellent in flavor and nutritional properties, so among the raw materials blended in the granules of the present invention, the barley green leaf dry powder content is preferably the highest.
- the specific gravity of the granules in the present invention means the bulk density (loose bulk density) measured with the granules gently filled in a container. -X; Hosokawa Micron Corporation).
- the specific gravity of the granulated product of the present invention is not particularly limited as long as it is in the range of less than 0.300 g/cm 3 , but the upper limit of the specific gravity is 0.295 g/cm 3 or less from the viewpoint of further improving the dispersibility.
- the lower limit of the specific gravity of the granulated product of the present invention is not particularly limited, it is preferably 0.100 g/cm 3 or more, more preferably 0.130 g/cm 3 or more, more preferably 0.130 g/cm 3 or more, from the viewpoint of further improving dispersibility. 140 g/cm 3 or more is more preferable, 0.150 g/cm 3 or more is particularly preferable, and 0.160 g/cm 3 or more is most preferable.
- the particle size distribution of the granules in the present invention means the weight-based particle size distribution, and can be measured using, for example, an electric sieve vibrator (MICRO VIBRO SIFTER M-2; Tsutsui Rikagakuki Co., Ltd.).
- the particle size distribution of the granulated product of the present invention is not particularly limited, but from the viewpoint of dispersibility, powder flowability, or ease of drinking, the particle size distribution of particles having a particle size of 500 ⁇ m or more is preferably 40% or less, and 30% or less. It is more preferably 25% or less, even more preferably 20% or less, particularly preferably 15% or less, and most preferably 10% or less.
- the particle size distribution with a particle size of 300 ⁇ m or more is preferably 50% or less, more preferably 40% or less, and 35% or less. More preferably, it is particularly preferably 30% or less, and most preferably 25% or less.
- the particle size distribution with a particle size of 300 ⁇ m or less is preferably 20% or more, more preferably 30% or more, and 40% or more. more preferably 50% or more, particularly preferably 60% or more, and most preferably 70% or more.
- the particle size distribution with a particle size of 150 ⁇ m or less is preferably 15% or more, more preferably 30% or more. It is more preferably 40% or more, particularly preferably 50% or more, and most preferably 60% or more.
- the particle size distribution with a particle size of 106 ⁇ m or less is preferably 15% or more, more preferably 30% or more. It is more preferably 40% or more, particularly preferably 50% or more, and most preferably 60% or more. Also, from the viewpoint of dispersibility, ease of handling (powder flow), or ease of drinking, the particle size distribution with a particle size of 106 ⁇ m or more is preferably 3% or more, more preferably 5% or more. It is more preferably 7% or more, particularly preferably 10% or more, and most preferably 15% or more.
- the granules of the present invention can be used as oral compositions.
- the form of the oral composition is not particularly limited, and includes, for example, foods and drinks, quasi-drugs, and pharmaceuticals. Since there are many, it is preferable to use it as a food-drinks composition.
- the form of the food and drink composition is not particularly limited, and examples thereof include food with function claims, food for specified health uses, and health food.
- the granules of the present invention are preferably used as powdered beverages because they are characterized by being easily dispersed in solvents such as water.
- a powdered drink means a processed food that is mixed with a liquid such as cold water, hot water, milk, or soybean milk for drinking. Powdered beverages have the advantage of being light in weight and easy to carry.
- Example 1 After feeding the green barley powder into a fluidized bed granulator, the green barley powder was fluidized by supplying air at 55° C., and intermittently sprayed with 75% by weight of water based on the weight of the green barley powder. Then, it was dried by supplying air at 120° C. to obtain the granulated product of Example 1 (with a water content of 5% by weight or less).
- Example 2 After feeding the green barley powder into a fluidized bed granulator, the green barley powder was fluidized by supplying air at 55° C., and then intermittently sprayed with 50% by weight of water based on the weight of the green barley powder. Then, it was dried by supplying air at 120° C. to obtain a granulated product of Example 2 (with a water content of 5% by weight or less).
- Comparative Example 1 After charging the young barley grass powder into an extrusion granulator, 10 to 30% by weight of water is appropriately added to the weight of the young barley grass powder to granulate, while taking care not to clog the screen (using a 1 mm screen), Drying temperature was set to 90° C. in a tray dryer to obtain granules of Comparative Example 1 (moisture content of 5% by weight or less).
- Comparative Example 2 was prepared by using non-granulated young barley powder.
- the granules of Examples 1 and 2 have a shorter dispersion time than the non-granulated young barley powder (Comparative Example 2) and are quickly dispersed in water. rice field.
- Granules containing green leaf dry powder of green juice material were produced by the method described below.
- Example 3 80% by weight of young barley powder produced in Test 1, 5% by weight of xylooligosaccharide, and 15% by weight of lactose were mixed to form a raw material. In the fluidized state, 50% by weight of water is intermittently sprayed with respect to the total weight of the raw materials, and then dried by supplying air at 100 ° C. to obtain the granulated product of Example 3 (moisture content: 5 weight % or less) was obtained.
- Example 4 After kale powder (pulverized and pulverized kale, median diameter 30 ⁇ m) is put into a fluidized bed granulator, the kale powder is fluidized by supplying air at 65 ° C., and the kale powder is 80% by weight of water was intermittently sprayed, followed by drying by supplying air at 80° C. to obtain granules of Example 4 (water content of 5% by weight or less).
- Example 5 After the Angelica keiskei powder (pulverized Angelica keiskei powder, median diameter 30 ⁇ m) was put into a fluidized bed granulator, the Angelica keiskei powder was fluidized by supplying air at 65 ° C., and the Angelica keiskei powder was obtained. 80% by weight of water was intermittently sprayed with respect to the weight of , and then dried by supplying air at 80° C. to obtain granules of Example 5 (water content of 5% by weight or less).
- Green tea powder (green tea powder obtained by pulverizing tencha [steamed green tea]; median diameter 30 ⁇ m) is put into a fluidized bed granulator, and then, in a state where the green tea powder is fluidized by supplying air at 75 ° C., green tea is processed. 30% by weight of water was intermittently sprayed with respect to the weight of powder, and then dried by supplying air at 120° C. to obtain granules of Comparative Example 5 (water content of 5% by weight or less).
- Example 6 Sweet potato young leaf powder (pulverized sweet potato leaves; median diameter: 30 ⁇ m) and green tea powder used in Comparative Example 6 were mixed so that each amount was 50% by weight. After that, while the raw material is fluidized by supplying air at 65°C, water is intermittently sprayed in an amount of 80% by weight with respect to the total weight of the raw material, and then dried by supplying air at 120°C. Granules of Example 6 (water content of 5% by weight or less) were obtained.
- Example 6 The young sweet potato powder used in Example 6 and the green tea powder used in Comparative Example 6 were mixed so that each amount was 50% by weight. After the raw material was put into a fluidized bed granulator, air at 80° C. was supplied. 20% by weight of water with respect to the total weight of the raw materials is intermittently sprayed while the raw materials are fluidized by doing so, and then dried by supplying air at 80 ° C. to obtain the granulated product of Comparative Example 6. (moisture content of 5% by weight or less) was obtained.
- Granules containing green leaf dry powder of green juice material were produced by the method described below.
- Example 7 60% by weight of mulberry leaf juice powder (squeezed powder obtained by adding dextrin to the mulberry leaf juice and spray-drying it to dry powder.
- the ratio of mulberry leaf juice and destrin is 1:1), and 40% by weight of reduced maltose.
- air at 70° C. is supplied to fluidize the raw materials, and 20% by weight of water is intermittently sprayed with respect to the total weight of the raw materials. Then, it was dried by supplying air at 100° C. to obtain a granulated product of Example 7 (with a water content of 5% by weight or less).
- Example 8 60% by weight of green barley juice powder (dextrin is added to the juice of young barley leaves and dried and powdered by spray drying. The ratio of young barley grass juice and dextrin is 1:1), and 40% by weight of reduced maltose.
- the raw materials mixed in are put into a fluidized bed granulator, the raw materials are fluidized by supplying air at 70 ° C., and 20% by weight of water is intermittently sprayed with respect to the total weight of the raw materials, and then and dried by supplying air at 100.degree.
- Example 9 Angelica keiskei powder (Ashitaba juice is added with dextrin and dried and powdered by spray drying. The ratio of Angelica keiskei juice and destrin is 1:1) 60% by weight, reduced maltose is 40% by weight After the raw materials mixed in are put into a fluidized bed granulator, the raw materials are fluidized by supplying air at 70 ° C., and 20% by weight of water is intermittently sprayed with respect to the total weight of the raw materials, and then and dried by supplying air at 100.degree.
- Granules containing green leaf dry powder of green juice material were produced by the method described below.
- Example 10 After the green barley powder (median diameter 18 ⁇ m) was put into a fluidized bed granulator, the green barley powder was fluidized by supplying air at 60° C., and 80% by weight of the green barley powder was added. Water was intermittently sprayed and then dried by supplying air at 100° C. to obtain granules of Example 10 (water content of 5% by weight or less). The granules of Example 10 had a specific gravity of 0.160 g/cm 3 and a particle size distribution of 150 ⁇ m or less of 60% or more. The granules of Example 10 were excellent in dispersibility and smoothness.
- Granules containing green leaf dry powder of green juice material were produced by the method described below.
- Example 11 After mulberry leaf powder (pulverized mulberry leaves, median diameter 30 ⁇ m) is put into a fluidized bed granulator, the mulberry leaf powder is fluidized by supplying air at 55 ° C. 80% by weight of water was intermittently sprayed with respect to the weight of , and then dried by supplying air at 120° C. to obtain granules of Example 11 (water content of 5% by weight or less).
- Example 12 Mugwort powder (made by pulverizing and pulverizing mugwort, median diameter 30 ⁇ m) is put into a fluidized bed granulator, and then, in a state where the mugwort powder is fluidized by supplying air at 55 ° C., the mugwort powder is added. 80% by weight of water was intermittently sprayed, followed by drying by supplying air at 120° C. to obtain granules of Example 12 (water content of 5% by weight or less).
- Example 13 Chomeisou powder (pulverized Chomeisou powder; median diameter: 30 ⁇ m) is put into a fluidized bed granulator, and then air is supplied at 55° C. to fluidize the Chomeisou powder. 80% by weight of water was intermittently sprayed with respect to the weight of the Chomeisou powder, and then dried by supplying air at 120°C to obtain the granules of Example 13 (water content of 5% by weight or less). .
- Example 14 After Kumazasa powder (pulverized and powdered Kumazasa, median diameter 30 ⁇ m) was put into a fluidized bed granulator, the Kumazasa powder was fluidized by supplying air at 55 ° C. 80% by weight of water was intermittently sprayed, followed by drying by supplying air at 120° C. to obtain granules of Example 14 (water content of 5% by weight or less).
- the granules of Examples 11 to 14 had a specific gravity of 0.280 g/cm 3 or less, and a particle size distribution of 150 ⁇ m or less in particle size distribution of 60% or more. All of these granules were excellent in dispersibility and smoothness.
- the granules of the present invention contain dry powder of at least one green leaf selected from barley, kale, sweet potato, mulberry, Angelica keiskei, mugwort, long-life grass, and kumazasa, and have excellent dispersibility and ease of drinking. Since it is an excellent granule and can be used as food and drink such as powdered beverages, it is highly industrially useful.
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Abstract
Description
[1]
麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の緑葉の乾燥粉末を含有する造粒物であって、比重が0.300g/cm3未満であることを特徴とする造粒物。
[2]
前記緑葉が麦類の緑葉であることを特徴とする[1]に記載の造粒物。
[3]
前記麦類が大麦であることを特徴とする[2]に記載の造粒物。
[4]
前記造粒物における前記緑葉の乾燥粉末の含有量が最も多いことを特徴とする[1]に記載の造粒物。
[5]
前記造粒物における前記緑葉の乾燥粉末の含有量が50重量%以上であることを特徴とする[1]に記載の造粒物。
[6]
前記造粒物における粒径500μm以上の粒度分布が10%以下であることを特徴とする[1]に記載の造粒物。
[7]
前記造粒物における粒径300μm以下の粒度分布が30%以上であることを特徴とする[1]に記載の造粒物。
[8]
経口組成物であることを特徴とする、[1]に記載の造粒物。
[9]
飲食品組成物であることを特徴とする、[1]に記載の造粒物。
[10]
麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の緑葉の乾燥粉末を含有する造粒物の製造方法であって、
前記緑葉の乾燥粉末を含む原料を流動層造粒機に投入し、空気を供給することによって前記原料を流動化させて水を噴霧した後、乾燥させて造粒物を得る工程を有し、
前記造粒物の比重が0.300g/cm3未満であることを特徴とする、造粒物の製造方法。
[11]
前記造粒物における粒径500μm以上の粒度分布が10%以下であることを特徴とする、[10]に記載の造粒物の製造方法
[12]
前記造粒物における粒径300μm以下の粒度分布が30%以上であることを特徴とする、[10]に記載の造粒物の製造方法。
[13]
前記噴霧する水の量が前記原料の合計重量に対して30重量%以上であることを特徴とする、[10]に記載の製造方法。
[14]
前記乾燥が90℃以上の空気を供給することによる乾燥であることを特徴とする、[10]に記載の製造方法。
[15]
50-75℃の空気を供給することによって前記原料を流動化させることを特徴とする、[10]に記載の製造方法。
[16]
前記噴霧が間欠噴霧であることを特徴とする、[10]に記載の製造方法。
本発明における青汁素材とは、麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の植物を意味する。1種のみを用いてもよいし、2種以上を用いてもよい。
本発明における麦類とは、大麦、小麦、ライ麦、えん麦など、外見の類似したイネ科植物の総称を意味する。本発明における麦類としては大麦が特に好ましい。
本発明におけるケールとは、アブラナ科アブラナ属であり、学名がBrassica oleracea var.acephalaである植物を意味する。ケールの品種としては、特に制限されるものではなく、キッチンケール、ツリーケール、ブッシュケール、マローケール、コラード、緑葉カンラン等の様々な種類のケールを用いることができる。ケールの緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明における甘藷とは、ヒルガオ科サツマイモ属であり、学名がIpomoea batatasである植物を意味する。甘藷は、一般にサツマイモと呼ばれるものであれば特に限定されない。甘藷の品種は、特に限定されず、例えば、すいおう、ジョイホワイト、コガネセンガン、シロユタカ、サツマスターチ、アヤムラサキなどの品種が挙げられる。なかでも、ポリフェノール含有量が高いすいおうが好ましい。甘藷の緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されないが、茎葉の先端部分(若茎葉)が好ましく、黄味がかった緑色を保持している状態の若茎葉がさらに好ましい。
本発明における桑とは、クワ科クワ属(Morus属)の植物を意味する。桑の種としては、特に限定されるものではなく、マグワ、ヤマグワ、ログワ、ナガミグワ、ケグワ、オガサワラグワ、テンジクグワ等を用いることができる。桑の緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明における明日葉とは、セリ科シシウド属であり、学名Angelica keiskeiである植物を意味する。明日葉の品種は、特に限定されず、適宜用いることができる。明日葉の緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明におけるヨモギとは、キク科ヨモギ属(Artemisia属)の多年草を意味する。ヨモギの種としては、特に限定されるものではなく、ヨモギ、ニガヨモギ、タラゴン、ニトロフヨモギ、オニオトコヨモギ、カワラヨモギ、オトコヨモギ、ハマヨモギ、カワラニンジン、クソニンジン、イヌヨモギ、ミヤマオトコヨモギ、エゾハハコヨモギ、サマニヨモギ、タカネヨモギ、ハハコヨモギ、シコタンヨモギ、シロヨモギ、イワヨモギ、ヒメヨモギ、ワタヨモギ、ケショウヨモギ、ヒトツバヨモギ、チシマヨモギ、ヒロハウラジロヨモギ、ヒロハヤマヨモギ、ユキヨモギ、ヤブヨモギ、オオヨモギ、ニシヨモギ、アサギリソウ、キタダケヨモギ等を用いることができるが、中でもヨモギが特に好ましい。ヨモギの緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明における長命草とはセリ科カワラボウフウ属であり、学名がPeucedanum japonicumである植物を意味する。長命草は地方によってボタンボウフウ、チョーメイソウ、チョーメイグサ、チョミーフサ、ボーフー、サクナ、ウプバーサフナ、チョーミーグサ、牡丹防風などと呼ばれている。長命草の品種は、特に限定されず、適宜用いることができる。長命草の緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明におけるクマザサとは、イネ科ササ属(Sasa属)の植物を意味する。クマザサの種としては、特に限定されるものではなく、Sasa veitchii、Sasa kurilensis、Sasamorpha borealis、Sasa senanensis、Sasa palmata、Sasa niponica等を用いることができる。クマザサの緑葉としては、いずれの収穫時期に収穫されたものであってもよく、特に限定されない。
本発明における緑葉の乾燥粉末とは、麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の緑葉を加工して乾燥粉末化したものを意味する。緑葉の乾燥粉末としては、例えば、緑葉を粉砕して乾燥粉末化したもの(緑葉の粉砕末)や緑葉の搾汁を乾燥粉末化したもの(緑葉の搾汁末)、緑葉の抽出物を乾燥粉末化したもの(緑葉のエキス末)等が挙げられるが、これらに限定されない。本発明の緑葉の乾燥粉末としては、分散性及び飲みやすさに優れる観点、加工、貯蔵、運搬等の容易性の観点、食物繊維を豊富に含むという観点から、緑葉の粉砕末であることが好ましい。
<造粒物>
造粒とは、複数の粒子を凝集させ、集合体を形成させる操作のことを意味する。前記集合体(造粒物)においては粒子が凝集する際に粒子間に空隙が形成されており、造粒物と造粒に用いる原料の粒子には構造的な違いがある。前記青汁素材の緑葉乾燥粉末を含有する造粒物とは、前記青汁素材の緑葉乾燥粉末を原料として造粒したものであり、比重が0.300g/cm3未満であることを特徴とする。
本発明における造粒物の比重とは、容器内へ造粒物を静かに充填した状態で計測した嵩密度(ゆるめ嵩密度)を意味し、例えば、粉体特性評価装置(パウダテスタ(R)PT-X;ホソカワミクロン株式会社)を用いて測定することができる。本発明の造粒物においては、比重を0.300g/cm3未満の範囲となるように制御することによって、分散性や飲みやすさに優れた造粒物を得ることができる。本発明の造粒物の比重としては0.300g/cm3未満の範囲であれば特に制限されないが、比重の上限としては、分散性をより向上させる観点から、0.295g/cm3以下が好ましく、0.290g/cm3以下がより好ましく、0.285g/cm3以下がさらに好ましく、0.280g/cm3以下がよりさらに好ましく、0.270g/cm3以下が特に好ましく、0.260g/cm3以下がより特に好ましく、0.250g/cm3以下が最も好ましい。本発明の造粒物の比重の下限値としては特に制限されないが、分散性をより向上させる観点から、0.100g/cm3以上が好ましく、0.130g/cm3以上がより好ましく、0.140g/cm3以上がさらに好ましく、0.150g/cm3以上が特に好ましく、0.160g/cm3以上が最も好ましい。
本発明における造粒物の粒度分布とは重量基準の粒度分布を意味し、例えば、電動篩振動機(MICRO VIBRO SIFTER M-2;筒井理化学器機株式会社 )を用いて測定することができる。本発明の造粒物における粒度分布は特に限定されないが、分散性、粉流れ、又は飲みやすさの観点から、粒径500μm以上の粒度分布が40%以下であることが好ましく、30%以下であることがより好ましく、25%以下であることがさらに好ましく、20%以下であることがよりさらに好ましく、15%以下であることが特に好ましく、10%以下が最も好ましい。また、分散性、粉流れ、又は飲みやすさの観点から、粒径300μm以上の粒度分布が50%以下であることが好ましく、40%以下であることがより好ましく、35%以下であることがさらに好ましく、30%以下であることが特に好ましく、25%以下であることが最も好ましい。
本発明の造粒物は、経口組成物として用いることができる。経口組成物の形態としては、特に制限されるものではなく、例えば、飲食品、医薬部外品、医薬品等が挙げられるが、青汁素材の緑葉の乾燥粉末は青汁として摂取されることが多いことから、飲食品組成物として用いることが好ましい。飲食品組成物の形態としては、特に制限されるものではなく、例えば、機能性表示食品、特定保健用食品、健康食品等が挙げられる。
[緑葉の乾燥粉末の製造]
原料として、背丈が約30cmで刈り取った大麦の地上部(葉及び茎)を用いた。これを水洗いし、付着した泥などを除去し、5-10cm程度の大きさに切断する前処理を行った。前処理した大麦若葉を、90-100℃の熱湯で90秒間-120秒間、1回のみブランチング処理し、その後、冷水で冷却した。続いて、得られた大麦若葉を、水分量が5重量%以下となるまで、乾燥機中で、20分間-180分間、80℃-130℃の温風にて乾燥させた。乾燥した大麦若葉を約1mmの大きさに粗粉砕処理した。得られた大麦若葉を微粉砕処理することにより、メディアン径20μmの大麦若葉末を製造した。
緑葉の乾燥粉末として前記製造方法で製造した大麦若葉末を用いた。以下に記載する方法により、緑葉の乾燥粉末を含有する造粒物を製造した。
大麦若葉末を流動層造粒機に投入後、55℃の空気を供給することによって大麦若葉末を流動化させた状態で、大麦若葉末の重量に対して75重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例1の造粒物(水分量5重量%以下)を得た。
大麦若葉末を流動層造粒機に投入後、55℃の空気を供給することによって大麦若葉末を流動化させた状態で、大麦若葉末の重量に対して50重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例2の造粒物(水分量5重量%以下)を得た。
大麦若葉末を押出し造粒機に投入後、スクリーン(1mmスクリーンを使用)の目詰まりに注意しながら大麦若葉末の重量に対して10-30重量%の水を適宜加水して造粒し、棚式乾燥機にて乾燥温度を90℃にして乾燥させ、比較例1の造粒物(水分量5重量%以下)を得た。
造粒していない大麦若葉末を比較例2とした。
以下に記載する方法により、実施例及び比較例について比重及び粒度分布を測定した。
粉体特性評価装置(パウダテスタ(R)PT-X;ホソカワミクロン株式会社)を用いて、被験物質を所定の高さから落下させて100cm3のステンレス製容器に入れ、質量を測定することにより比重を測定した。測定結果を表1に示す。
電動篩振動機(MICRO VIBRO SIFTER M-2;筒井理化学器機株式会社)を用いて粒度分布を測定した。測定結果を表2に示す。
以下に記載する(1)及び(2)の方法により、実施例及び比較例について分散性を評価した。
(1)-1.水にサンプルを投与した際における分散性
100mLの水を入れたコップ(高さ100mm、上部の直径75mm、底部の直径55mm)に各サンプル3gずつを静かに投入し、サンプルを投下してからサンプル全体が水に浸漬して水中に分散するまでの時間(液面に浮遊した状態から水中に沈むまでの時間)を分散時間として測定し、以下の基準にしたがって水なじみを評価した。結果を表3に示す。「水なじみ」とは、粉体の水への濡れ性をいう。
<基準>
〇:分散時間が60秒未満
×:分散時間が60秒以上
各サンプル3gずつを入れたコップ(高さ100mm、上部の直径75mm、底部の直径55mm)に、水100mLを静かに注ぎ込んだ。その後、水面を観察し、以下の基準にしたがって粉浮きの有無を評価した。結果を表4に示す。「粉浮き」とは、水面への粉体の浮きやすさをいう。
<基準>
有:サンプルの少なくとも一部が水面に浮いている
無:サンプルが水面に浮いていない(水中に分散又は沈んでいる)
100mLの水を入れた円柱状(直径75mm)の透明なコップに各サンプル3gをそれぞれ投入し、マドラーを用いて10回攪拌(攪拌速度は1~1.5回/秒)した。各サンプルは不溶性であるため、攪拌によって水中に一時的には分散するが、時間が経過すると徐々に沈降し、上の方に澄んだ部分(上澄み)ができる。攪拌を完了してから1分間静置した後、コップの中身を観察し、上澄みの高さ(分離距離)を測定し、以下の基準にしたがって分散安定性を評価した。分離距離が短いほど、サンプルが水に安定な状態で分散しており、分離しにくいことを意味する。測定結果を表5に示す。
<基準>
〇:分散距離が5mm未満
×:分散距離が5mm以上
<分散性の総合評価>
〇:水なじみ「〇」、かつ、粉浮きの有無「無」、かつ、分散安定性「〇」、である場合
×:上記以外の場合
各サンプル3gを100mLの水を入れたコップに投入した。投入後、マドラーを用いて10回攪拌(攪拌速度は1~1.5回/秒)した。その後すぐに各飲料を摂取し、以下の基準にてのど越しを評価した。結果を表7に示す。
<基準>
〇:飲用時にのどにイガイガを全く感じない又はイガイガをほとんど感じない
×:飲用時にのどにイガイガを感じる
各サンプル3gをアルミニウムパウチの分包に充填した。得られたサンプル入り分包を用いて、分包開封時の粉舞い、コップへの投入時の粉流れ(取扱いのしやすさの指標)について基準にしたがって評価し、取扱性を確認した。結果を表8に示す。
<基準>
開封時の粉舞い。「粉舞い」とは、空気中への粉体の舞いやすさをいう。
〇:分包の開封時に粉舞いが少ない
×:分包の開封時に粉舞いが多い
投入時の粉流れ。「粉流れ」とは、粉体の流れやすさをいう。
〇:コップに投入する際の粉流れがスムーズである
×:コップに投入する際の粉流れがスムーズでない
上述した試験により、大麦若葉末を含有し、比重が0.300g/cm3未満である造粒物(実施例1及び2)は、分散性、のど越し、取扱性がいずれも優れていた。一方、大麦若葉末を含有し、比重が0.300g/cm3を超える造粒物(比較例1)は、取扱性は優れているが、分散性及びのど越しは悪かった。また、造粒していない大麦若葉末(比較例2)は、のど越しは優れているが、分散性及び取扱性は悪かった。したがって、大麦若葉末を含有し、比重が0.300g/cm3未満の造粒物は、分散性、のど越し、取扱性に優れたものであることが明らかとなった。
[緑葉の乾燥粉末を含有する造粒物の製造]
以下に記載する方法により、青汁素材の緑葉乾燥粉末を含有する造粒物を製造した。
試験1で製造した大麦若葉末80重量%、キシロオリゴ糖5重量%、乳糖15重量%となるように混合した原料を流動層造粒機に投入後、70℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して50重量%の水を間欠噴霧し、その後、100℃の空気を供給することにより乾燥させて実施例3の造粒物(水分量5重量%以下)を得た。
試験1で製造した大麦若葉末80重量%、キシロオリゴ糖5重量%、乳糖15重量%となるように混合した原料を流動層造粒機に投入後、80℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して10重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて比較例3の造粒物(水分量5重量%以下)を得た。
ケール末(ケールを粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、65℃の空気を供給することによってケール末を流動化させた状態で、ケール末の重量に対して80重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて実施例4の造粒物(水分量5重量%以下)を得た。
明日葉末(明日葉を粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、65℃の空気を供給することによって明日葉末を流動化させた状態で、明日葉末の重量に対して80重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて実施例5の造粒物(水分量5重量%以下)を得た。
実施例5と同じ明日葉末を流動層造粒機に投入後、80℃の空気を供給することによって明日葉末を流動化させた状態で、明日葉末の重量に対して10重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて比較例4の造粒物(水分量5重量%以下)を得た。
緑茶末(碾茶[蒸し製緑茶]を粉末化した抹茶末。メディアン径30μm)を流動層造粒機に投入後、75℃の空気を供給することによって緑茶末を流動化させた状態で、緑茶末の重量に対して30重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて比較例5の造粒物(水分量5重量%以下)を得た。
甘藷若葉末(甘藷の葉を粉砕処理して粉末化したもの。メディアン径30μm)、比較例6に用いた緑茶末がそれぞれ50重量%となるように混合した原料を流動層造粒機に投入後、65℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して80重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例6の造粒物(水分量5重量%以下)を得た。
実施例6に用いた甘藷若葉末、比較例6に用いた緑茶末がそれぞれ50重量%となるようにとなるように混合した原料を流動層造粒機に投入後、80℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して20重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて比較例6の造粒物(水分量5重量%以下)を得た。
試験1と同じ方法により、実施例及び比較例について比重及び粒度分布を測定した。結果を表9に示す。
試験1と同じ方法により分散性及び飲みやすさ(のど越し)を評価した。結果を表9に示す。
大麦若葉末、ケール末、明日葉末又は甘藷若葉末を含有し、比重が0.300g/cm3未満である造粒物(実施例3-6)は、分散性及びのど越しが優れていた。一方、大麦若葉末、明日葉末又は甘藷若葉末を含有していても、比重が0.300g/cm3以上の造粒物には、のど越しは優れるものの、分散性は悪かった(比較例3、4、6)。また、緑茶末からなる造粒物は、比重が0.300g/cm3未満であっても、分散性及びのど越しは悪かった(比較例5)。
[緑葉の乾燥粉末を含有する造粒物の製造]
以下に記載する方法により、青汁素材の緑葉乾燥粉末を含有する造粒物を製造した。
桑葉搾汁末(桑葉の搾汁液にデキストリンを加えてスプレードライにより乾燥粉末化した搾汁末。桑葉搾汁液とデストリンの比率は1:1)60重量%、還元麦芽糖40重量%となるように混合した原料を流動層造粒機に投入後、70℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して20重量%の水を間欠噴霧し、その後、100℃の空気を供給することにより乾燥させて実施例7の造粒物(水分量5重量%以下)を得た。
実施例7で用いた桑葉搾汁末60重量%、還元麦芽糖40重量%となるように混合した原料を流動層造粒機に投入後、80℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して20重量%の水を間欠噴霧し、その後、80℃の空気を供給することにより乾燥させて比較例7の造粒物(水分量5重量%以下)を得た。
大麦若葉搾汁末(大麦若葉の搾汁液にデキストリンを加えてスプレードライにより乾燥粉末化したもの。大麦若葉搾汁液とデストリンの比率は1:1)60重量%、還元麦芽糖40重量%となるように混合した原料を流動層造粒機に投入後、70℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して20重量%の水を間欠噴霧し、その後、100℃の空気を供給することにより乾燥させて実施例8の造粒物(水分量5重量%以下)を得た。
明日葉搾汁末(明日葉の搾汁液にデキストリンを加えてスプレードライにより乾燥粉末化したもの。明日葉搾汁液とデストリンの比率は1:1)60重量%、還元麦芽糖40重量%となるように混合した原料を流動層造粒機に投入後、70℃の空気を供給することによって原料を流動化させた状態で、原料の合計重量に対して20重量%の水を間欠噴霧し、その後、100℃の空気を供給することにより乾燥させて実施例9の造粒物(水分量5重量%以下)を得た。
試験1と同じ方法により、実施例及び比較例について比重及び粒度分布を測定した。結果を表10に示す。
試験1と同じ方法により分散性及び飲みやすさ(のど越し)を評価した。結果を表10に示す。
桑葉搾汁末、大麦若葉搾汁末、又は明日葉搾汁末を含有し、比重が0.300g/cm3未満である造粒物(実施例7-9)は、分散性及びのど越しが優れていた。一方、桑葉搾汁末を含有し、比重が0.300g/cm3以上の造粒物は、のど越しは優れるものの、分散性は悪かった(比較例7)。
[緑葉の乾燥粉末を含有する造粒物の製造]
以下に記載する方法により、青汁素材の緑葉乾燥粉末を含有する造粒物を製造した。
大麦若葉末(メディアン径18μm)を流動層造粒機に投入後、60℃の空気を供給することによって大麦若葉末を流動化させた状態で、大麦若葉末の重量に対して80重量%の水を間欠噴霧し、その後、100℃の空気を供給することにより乾燥させて実施例10の造粒物(水分量5重量%以下)を得た。実施例10の造粒物は比重0.160g/cm3であり、粒径150μm以下の粒度分布が60%以上であった。実施例10の造粒物は、分散性及びのど越しが優れていた。
[緑葉の乾燥粉末を含有する造粒物の製造]
以下に記載する方法により、青汁素材の緑葉乾燥粉末を含有する造粒物を製造した。
桑葉末(桑葉を粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、55℃の空気を供給することに桑葉末を流動化させた状態で、桑葉末の重量に対して80重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例11の造粒物(水分量5重量%以下)を得た。
ヨモギ末(ヨモギを粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、55℃の空気を供給することにヨモギ末を流動化させた状態で、ヨモギ末の重量に対して80重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例12の造粒物(水分量5重量%以下)を得た。
長命草末(長命草を粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、55℃の空気を供給することに長命草末を流動化させた状態で、長命草末の重量に対して80重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例13の造粒物(水分量5重量%以下)を得た。
クマザサ末(クマザサを粉砕処理して粉末化したもの。メディアン径30μm)を流動層造粒機に投入後、55℃の空気を供給することにクマザサ末を流動化させた状態で、クマザサ末の重量に対して80重量%の水を間欠噴霧し、その後、120℃の空気を供給することにより乾燥させて実施例14の造粒物(水分量5重量%以下)を得た。
Claims (4)
- 麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の緑葉の乾燥粉末を含有する造粒物であって、比重が0.300g/cm3未満であることを特徴とする造粒物。
- 前記緑葉が麦類の緑葉であることを特徴とする請求項1に記載の造粒物。
- 前記造粒物における粒径500μm以上の粒度分布が10%以下であることを特徴とする請求項1または2に記載の造粒物。
- 麦類、ケール、甘藷、桑、明日葉、ヨモギ、長命草及びクマザサから選ばれる少なくとも1種の緑葉の乾燥粉末を含有する造粒物の製造方法であって、
前記緑葉の乾燥粉末を含む原料を流動層造粒機に投入し、空気を供給することによって前記原料を流動化させて水を噴霧した後、乾燥させて造粒物を得る工程を有し、
前記造粒物の比重が0.300g/cm3未満であることを特徴とする、造粒物の製造方法。
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JP2008086311A (ja) * | 2006-09-08 | 2008-04-17 | Fancl Corp | 緑色野菜青汁用粉末及びその製造方法 |
JP2015002715A (ja) * | 2013-06-21 | 2015-01-08 | 株式会社大石茶園 | 桑葉加工品及びその製造方法 |
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JP2005328843A (ja) * | 2004-04-22 | 2005-12-02 | Nippon Kayaku Food Techno Kk | 凝集沈殿が改善されたキトサン含有緑葉組成物及び飲料 |
JP2008086311A (ja) * | 2006-09-08 | 2008-04-17 | Fancl Corp | 緑色野菜青汁用粉末及びその製造方法 |
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