JP2005269990A - Method for extracting mushroom essence, method for producing mushroom essence product, mushroom essence, and mushroom essence product - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for extracting mushroom essence capable of efficiently extracting an active ingredient in an improved essence yield, and to provide a method for producing a mushroom essence product. <P>SOLUTION: The method for extracting mushroom essence comprises extracting a mushroom carpophore essence soluble to hydrous ethanol with the hydrous ethanol 30-90 wt.% in concentration at 30-80°C from a mushroom carpophore ground product. In this method, the bulk density of the ground product is preferably ≥0.2 g/cm<SP>3</SP>. The method for producing the mushroom essence product comprises heating the essence-containing hydrous ethanol at a temperature lower than the boiling point to remove ethanol followed by grinding the resultant essence to obtain essence powder, which is used. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a method for extracting persimmon extract including perennial persimmon, a method for producing a persimmon extract product, a persimmon extract, and a persimmon extract product.

The perennial moth is a moss also known as Saiwaitake, also called the Reishi in the Chinese name, and has been traditionally used for viewing floor decorations.
In recent years, the medicinal effect of Ganoderma has attracted attention, and Ganoderma is provided as a health supplement in the form of granules, tablets and the like.

  To cultivate perennial rice cake, a mixture of sawdust, rice bran, bran, etc. (referred to as the culture medium) is filled in a container such as a culture bag or a wide-mouth bottle, and then the fungus is planted in this culture medium. Incubate for a period. Then, the fungus (mycelium) spreads in the medium in the container, and a so-called fungus bed is obtained. By maintaining this fungus bed in a predetermined range of humidity, temperature, and illuminance environment, a perennial fruit body grows from the fungus bed. . Then, the grown fruit body is harvested and subjected to processes such as pulverization, extract extraction, and pulverization to obtain a health supplement in the form of granules, tablets, capsules, and the like.

By the way, in the extract extraction process, water, alcohol, or hydrous alcohol is used to extract water-soluble and alcohol-soluble active ingredients.
For example, in the technique described in Patent Document 1, cold hydrous alcohol is added to a ground product of a reishi fruit body to extract a hydrous alcohol-soluble component. Moreover, in the technique described in Patent Document 2, the active ingredient is extracted with hot water or an aqueous alcohol solution from the extraction residue after extraction of ganoderma with a nonpolar solvent. In the technique described in Patent Document 3, a two-stage process comprising extraction of a hydrous alcohol-soluble component with a hydrous alcohol having a concentration of 30 to 70 [%] and extraction of a water-soluble component of hot water into a pulverized product of a ganoderma fruit body. Extraction.

JP 2003-235502 A Japanese Patent No. 3128147 Japanese Patent No. 2965490

In such an extract extraction process, it is desired to increase the total yield of the extract and to efficiently extract specific components such as triterpenes. However, in the technique described in Patent Document 1, the total yield of the extract is low and the extraction amount of triterpenes is low. Moreover, in the technique described in Patent Document 2, triterpenes, which are effective components of ganoderma, are removed by using a nonpolar solvent. Furthermore, the extraction process using a nonpolar solvent, the extraction process using hot water or an aqueous alcohol solution, and the two-stage extraction process are performed, and there is a problem that the process is complicated. The technique described in Patent Document 3 also has a problem that the two-stage extraction process is complicated, the process is complicated, and the extract yield remains as low as 8.51 to 9.54 [%]. .
The present invention has been made on the basis of such a technical problem. The extraction method for moss extract and the method for producing the moss extract product capable of improving the extract yield and efficiently extracting the active ingredient. The purpose is to provide.

The extraction method of the moss extract of the present invention comprises a pulverization step of pulverizing the fruit bodies of moss and a ground product of the pulverized fruit bodies having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C]. An extraction step of extracting a hydrous alcohol-soluble extract of a fruit body with a hydrous alcohol, and a removal step of removing the alcohol by heating the hydrous alcohol containing the extract below the boiling point following the extraction step. And
Extracts can be efficiently extracted by pulverizing the fruit bodies of persimmons such as perennial persimmons with water-containing alcohol having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C]. If the extract yield is to be increased, the alcohol concentration is preferably 30 to 80 [%]. If the polyphenol extraction efficiency is to be increased, it is preferably 30 to 90 [%], more preferably 60 to 70 [%]. The alcohol concentration is preferable. If the amount of a.alcohol is increased, the alcohol concentration is preferably 40 to 85 [%].
At this time, the extraction of the extract is performed only in one step with the hydrous alcohol satisfying the above conditions. That is, the extraction of the extract is completed by putting the pulverized material obtained by pulverizing the fruit body into the hydrous alcohol for a predetermined time.

  By the way, in the pulverization step or the like, it is preferable to manage the pulverization level of the fruit body. Conventionally, for example, a length such as “2 to 20 [mm]”, a particle size, and a mesh size of a sieve are used (for example, refer to Patent Documents 4, 5, and 6).

JP-A-9-56362 (page 3, paragraph [0016]) JP 2003-121788 A (Claim 1 etc.) Japanese Patent Laid-Open No. 5-13989 (Claim 1 etc.)

However, it is difficult to completely destroy fibers even if pulverized, such as a perennial cocoon, consisting of a collection of hyphae. Therefore, the pulverized pulverized product does not have a shape close to a spherical shape or a lump shape, but has an irregular shape such as a needle shape or a cotton shape in which fibers are tangled.
For this reason, even if the length is measured, it is difficult to accurately measure in the longitudinal direction of the irregularly pulverized product. Even when the particle size is used, it is difficult to accurately measure the particle size of the irregularly shaped measurement object (pulverized product) with the particle size distribution meter used for measuring the particle size. When using a mesh size, it will actually be determined whether or not it will pass through a sieve having a predetermined mesh size, but the acicular pulverized material may or may not pass through the sieve mesh depending on its direction. Therefore, accurate evaluation is difficult even with this method.
As described above, in the conventional technique, it is difficult to accurately evaluate the pulverization level of the pulverized product, and it cannot be said that the pulverization level is substantially controlled. In the case of fountain lees etc., the pulverization level of the pulverized product affects the yield of the active ingredient obtained, so it can be said that there is room for improvement in the yield of the active ingredient.

Therefore, in the present invention, the bulk density is used for evaluating the pulverization level of the pulverized product.
In the extraction process, when the extract is extracted from the pulverized product having a bulk density of 0.2 [g / cm ³ ] or more, the extract yield is remarkably improved and the extract yield is extracted by 10 [%] or more. The amount of polyphenol can be 4 [mg / g fruiting body] or more. Here, the unit [mg / g fruiting body] of the amount of polyphenol is the content [mg] of polyphenol in the fruiting body 1 [g].
The extract extracted by such a method may be used for any purpose. However, when the extract is edible / drinkable, it is preferable to use ethanol as the alcohol.

The present invention relates to a pulverization step of pulverizing a fruit body of a moss, and hydrous ethanol having an ethanol concentration of 30 to 90 [%] and 30 to 80 [° C.] Extracting the water-soluble ethanol-soluble extract, and following the extraction step, the water-containing ethanol containing the extract is heated at the boiling point or less, the ethanol is removed, and the extract is powdered. It can be understood as a method for producing a moss extract product characterized by having a product formation step for forming a moss extract product. Here, moss extract products include forms such as capsules, tablets, granules, powders, and drinks.
In this case, in the pulverization step, the fruit body is preferably pulverized until the bulk density of the pulverized material of the fruit body becomes 0.2 [g / cm ³ ] or more.

The present invention can also be understood as an extract of moss extracted from a pulverized product obtained by pulverizing a fruit body of moss. In this case, the moss extract is characterized in that the extract yield from the fruiting body is 10 [%] or more and the amount of extracted polyphenol is 4 [mg / g fruiting body] or more. Furthermore, the amount of Ganoderic Alcohols extracted from the fruiting body may be 500 [μg / g fruiting body] or more.
Such a moss extract can be extracted from the pulverized product with a hydrous alcohol having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C.].

  The present invention relates to a moss extract product obtained by extracting a moss extract from a pulverized product obtained by pulverizing a fruit body of a moss, and having an ethanol concentration of 30 to 90 [%]. The raw material is an extract obtained by extraction from a pulverized product with hydrous ethanol at 30 to 80 [° C.].

  The moss targeted by the present invention is mainly a perennial moth. In addition, for example, shiitake mushrooms, sea cucumbers, oyster mushrooms, shimeji mushrooms, enoki mushrooms, jellyfish, maitake mushrooms, shirohirotake mushrooms, choi maitake mushrooms, moss mushrooms, kawatake mushrooms, mesima mushrooms, agaricus s. The present invention can also be applied to these moss species. Further, among these, the present invention is particularly suitable for moss of the moss family, Meshimakobu, etc., among which the fiber is hard.

According to the method of the present invention, an extract is extracted with hydrous alcohol having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C.] from a pulverized fruit body of persimmon such as perennial cocoon, Extract yield can be improved and active ingredients can be extracted efficiently.
In addition, the moss extract and moss extract product obtained by such a method may contain active ingredients such as extract and polyphenol at a higher yield than those obtained by conventional methods. It becomes possible.

Hereinafter, the present invention will be described in detail based on embodiments shown in the accompanying drawings.
FIG. 1 is a diagram for explaining the flow of the extraction process of moss extracts and the production process of moss extracts in the present embodiment.
The fruiting body for extracting Ganoderma mosquito extract is maintained in a predetermined range of humidity, temperature, and illuminance, with the fungus planted in the medium and cultivated for a certain period of time. It is obtained by doing. From the fungus bed, a perennial deer horn-shaped fruit body (so-called deer anteater) grows. When this fruiting body is cut out from the fungus bed and dried for a predetermined period of time, a dried fruiting body is obtained. From this dried fruiting body, ganoderma extract is extracted as follows.

<Crushing process>
A dried fruit body (hereinafter simply referred to as a fruit body) is coarsely pulverized by a crushing device with a rotary blade or the like, and then finely pulverized by a pulverizing means such as a dry jet mill.
Here, in the present embodiment, it is preferable to manage the pulverization level of the fruit body based on the bulk density.

In principle, as shown in FIG. 2, the bulk density is such that the finely pulverized product 10 is poured from above into a container 1 having a predetermined volume so as to rise above the upper end surface 1 a of the container 1. At this time, in order to prevent the excessively pulverized product 10 from being mixed, the pulverized product 10 poured into the container 1 is preferably passed through a sieve having a predetermined mesh size. Then, the finely pulverized product 10 rising from the upper end surface 1a is slid along the upper end surface 1a of the container 1 by the plate 2 or the like. Thereafter, the weight density X of the finely pulverized material 10 remaining in the container 1 is measured and divided by the volume V of the container 1 to obtain a bulk density X.
X = W / V [g / cm ³ ]

  In the present embodiment, it is preferable to perform fine grinding until the bulk density X satisfies X ≧ 0.2. Thus, the extract yield can be increased by making the pulverization level of the finely pulverized product finer than a predetermined level.

<Extraction process>
The obtained finely pulverized product is extracted with an active ingredient such as β-glucan from the finely pulverized product by extraction with hydrous ethanol. Here, as the hydrous ethanol used for extraction, warm hydrous ethanol having an ethanol concentration of 30 to 90 [%] and a temperature of 30 to 80 [° C.] is used. Thereby, the hydrous alcohol soluble component is extracted from the finely pulverized product.
After extraction of the active ingredient from the finely pulverized product, the extraction of the extract itself is completed by evaporating and drying ethanol at a temperature below the boiling point (under normal pressure or reduced pressure).
In addition, the extract extracted in this way can be stored as a solution at -20 [° C.], or it can be stored as a solid by freeze-drying, vacuum concentration, or the like.

<Powdering process>
The extracted residue is added to the extracted extract to obtain a slurry-like extract. Then, the slurry-like extract is pulverized with a spray dryer or the like to obtain an extract powder.

<Product formation process>
The obtained extract powder is weighed and filled into a capsule to produce a capsule-like moss extract product. Moreover, a tablet-like moss extract product can be formed by mixing a binder or the like with a predetermined weight of the extract powder and performing tableting with a predetermined shape. Of course, in addition to capsules and tablets, it is of course possible to form fine powder or granules of a predetermined particle size when powdered, or to mix this with a liquid to make a drink.

Thus, in the extract extraction step, the extract yield can be increased by using warm hydrous ethanol having an ethanol concentration of 30 to 90 [%] and a temperature of 30 to 80 [° C.]. In particular, active ingredients such as triterpenes and polyphenols can be efficiently extracted. In addition, the extraction is only one stage with water-containing ethanol, and it is not necessary to perform the two-stage extraction as in the conventional case, so that the extraction can be easily performed.
Furthermore, the above-mentioned effect becomes even more remarkable by performing extract extraction from a finely pulverized product having a bulk density X of X ≧ 0.2, more preferably X ≧ 0.25.

Here, since the evaluation of the pulverization level of the finely pulverized product was performed using the bulk density and the case where the pulverized product was performed using the conventional particle size distribution, the results are shown.
After harvesting, the dried deer anteater was coarsely pulverized to about 3 mm, and then finely pulverized with a dry jet mill to obtain a finely pulverized product. Here, the supply speed of the coarsely pulverized product after the coarse pulverization to the dry jet mill,
Test 1: 5.0 [kg / Hr]
Test 2: 3.5 [kg / Hr]
Test 3: 2.5 [kg / Hr]
Test 4: 1.5 [kg / Hr]
Test 5: 0.5 [kg / Hr]
Thus, five kinds of finely pulverized products having different pulverized states were obtained.
In other words, the time required for processing a coarsely pulverized product of 10 [kg] (grinding time) is:
Test 1: 2 hours Test 2: 2 hours 50 minutes Test 3: 4 hours Test 4: 6 hours 42 minutes Test 5: 20 hours.

The finely pulverized product obtained as described above was fixed on a carbon tape, and was further sputter coated with Pt-Pd to prevent electrification, and was observed with a scanning electron microscope (SEM) (acceleration during observation). Voltage: 0.5 kV, emission current 5 nA).
3A is an SEM photograph of a finely pulverized product obtained by Test 1, FIG. 3B is Test 2, FIG. 4A is Test 3, FIG. 4B is Test 4, and FIG. 5 is Test 5.

  As is clear from these SEM photographs, the finely pulverized powder obtained as the feed rate of the coarsely pulverized product to the dry jet mill is lowered, that is, the pulverization time is increased and the pulverization time in the dry jet mill is increased. It is clear visually that the particles of the object become finer.

The bulk density of the finely pulverized products of Test 1 to Test 5 thus obtained was measured. For this purpose, the finely pulverized product is dropped into a measuring cell (container 1) having a volume of 20 [ml] through a sieve of 42 mesh openings, the weight of the finely pulverized product per 20 [ml] is measured, and the bulk density is measured. Was calculated.
For comparison, the finely pulverized product of Test 1 to Test 5 was dispersed in methanol using ultrasonic waves, and the particle size distribution of the finely pulverized product was measured with a laser diffraction particle size distribution analyzer.
The results are shown in Table 1.

  As shown in Table 1, the finely pulverized product of Test 1 to Test 5 is a measurement result of the particle size distribution although the difference in the pulverization level can be clearly confirmed in the SEM photographs shown in FIGS. Thus, both the average particle size and the particle size distribution were almost the same for the finely pulverized products of Test 1 to Test 5.

In contrast, the bulk density is
Test 1: 0.18 [g / cm ³ ]
Test 2: 0.22 [g / cm ³ ]
Test 3: 0.26 [g / cm ³ ]
Test 4: 0.28 [g / cm ³ ]
Test 5: 0.35 [g / cm ³ ]
Are clearly different between the finely pulverized products of Test 1 to Test 5, and similarly to the SEM photographs shown in FIGS. 3 to 5, the supply speed of the coarsely pulverized product to the dry jet mill is lowered, that is, the pulverization time is lengthened. There is a correlation that the longer the time of pulverization in the dry jet mill, the greater the bulk density of the finely pulverized product obtained.

  In this way, it is difficult to completely destroy the fiber even when pulverized, such as a perennial cocoon sample, and it becomes cotton-like or needle-like. The distribution confirmed that the true particle size could not be evaluated. On the other hand, it was confirmed that the bulk density corresponded well to the crushing level of the SEM photograph, and that the crushing level of the fountain cake could be quantified and accurately evaluated.

  Moreover, in the finely pulverized product of Test 5 shown in FIG. 5, it was confirmed that the mycelium of the perennial silkworm was almost completely crushed. That is, by setting the bulk density to about 0.35, it can be said that a finely pulverized product in which perennial mycelia are almost completely crushed can be obtained.

After pulverization, the extract was extracted by hot water extraction at 100 [° C.] for 1 hour. Then, the extract was filtered through a membrane filter, and the filtrate was evaporated to dryness. Then, the weight was measured, and this was defined as the extract yield.
The result is shown in FIG.

As shown in FIG. 6, the yield of the water-soluble extract is almost constant when the bulk density is less than 0.2 [g / cm ³ ], but when it becomes 0.2 [g / cm ³ ] or more, It was confirmed that the yield of the extract was increased.

  In this way, the pulverization level can be accurately evaluated by using the bulk density in the process of extracting the extract from the perennial fruit body. This makes it possible to manage the yield of the active ingredient obtained in the mass production process, and to improve the yield of the active ingredient more than before. Furthermore, since the pulverization level can be accurately evaluated, the quality of granules, tablets, capsules and the like produced from finely pulverized products whose pulverization level is controlled within a certain range can be stabilized more than ever.

Moreover, since the relationship between the density | concentration of the water-containing ethanol used for extraction and an extract yield was investigated, the result is shown below.
After harvesting, the dried deer anteater was coarsely pulverized to about 3 [mm] square, and then finely pulverized by a dry jet mill, so that the bulk density was 0.2 [g / cm ³ ] or more. For the measurement of the bulk density, a finely pulverized product is dropped into a measurement cell having a volume of 20 [ml] through a sieve of 42 mesh openings, and the weight of the finely pulverized product per volume of 20 [ml] is measured. Was calculated.
Thereafter, the finely pulverized product 4 [g] was added to 100 [ml] of water-containing ethanol diluted with distilled water and heated for 1 hour with stirring in a water bath at 60 [° C.] to extract the extract. It was. Here, the ethanol concentration was 0 (ie, hot water extraction using water), 30, 40, 50, 60, 65, 70, 75, 80, 85, 90, 100 (ie, ethanol extraction) [%]. .
The extract yield was measured by weight after filtering the extract with a membrane filter and evaporating the filtrate to dryness.
The result is shown in FIG.

  As shown in FIG. 7, in the case of hot water extraction not containing ethanol, or when the ethanol concentration is too low or too high, the extract yield becomes low, and the ethanol concentration is 30 to 80%. It was confirmed that a high extract yield was obtained in the range.

Moreover, since it evaluated about the quantity of the triterpenes obtained by extract extraction, the result is shown below.
Extracts were extracted from the finely pulverized product obtained in the same manner as in Example 2 at different ethanol concentrations. The extract obtained by the extract extraction was subjected to solid-liquid separation and divided into an extract and an extraction residue. And after evaporating the extract to dryness, triterpenes were dissolved and collected using 100% methanol, and after concentration under reduced pressure, the amount of triterpenes was measured by HPLC (high performance liquid chromatography). The analysis conditions in HPLC are as follows.
Column Tosoh TSK-GEL ODS-80TM (4.6φ × 15 [mm])
Mobile phase Ganoderic Alcohol Fr. Acetonitrile: 2 [%] Acetic acid 60:40
Ganoderic Acid Fr. Acetonitrile: 2 [%] Acetic acid 30:70
Flow rate 1 [ml / min]
HPLC system Hitachi D-7000 HSM

FIGS. 8A and 8B show the amount of Ganoderic Alcohols or Ganoderic Acids contained in the extract when water-containing ethanol adjusted to each concentration is used as an extraction solvent.
As a result, the amount of Ganoderic Alcohol extracted from the extract was high when the ethanol concentration of hydrous ethanol was 40 [%] or higher, and the amount of Ganoderic Acid was high when 30 [%] or higher.
In the extraction process and the step of removing ethanol, the triterpenes were decomposed when heated to a temperature higher than the boiling point of hydrous ethanol.

  Thereby, in order to raise the extraction amount of triterpenes, it was confirmed that the ethanol concentration of the water-containing ethanol used for the extraction extraction is preferably 30 to 40 [%] or more and the upper limit is preferably less than the boiling point.

Next, the relationship between the ethanol concentration of hydrous ethanol used for extraction and the total polyphenol content of the extract obtained was examined, and the results are shown below.
The total polyphenol content of the extract obtained in Example 2 was measured by the Forindennis method, the presence of the phenolic hydroxyl group was converted to the catechin content, and the content in the fruit body 1 [g] [mg / g fruit body] Calculated as
The result is shown in FIG.
As shown in FIG. 9, by setting the ethanol concentration of the water-containing ethanol used for the extraction to 30 to 90 [%], the polyphenol extraction amount increases, and in particular, the ethanol concentration is set to 60 to 70 [%]. Thus, it was confirmed that the amount of polyphenol extracted was particularly high.

Finely pulverized product 4 [g] obtained in the same manner as in Example 2 was added to 100 [ml] hydrous ethanol diluted with distilled water to an ethanol concentration of 70 [%], and the temperature (extraction temperature) was 25 [room temperature]. The extract was extracted by heating for 1 hour with stirring in a water bath adjusted to 90 ° C.
The total polyphenol content of the obtained extract was measured by the Folin dennis method, and the presence of the phenolic hydroxyl group was converted to the catechin content and calculated as the content in the fruit body 1 [g].
The result is shown in FIG.

As shown in FIG. 10, both the extract yield and the amount of polyphenol extracted were higher at a temperature higher than 25 [° C.] at room temperature, and there was not much difference at a temperature higher than 80 [° C.] that is higher than the boiling point of ethanol.
As a result, it is confirmed that the extract extraction is performed at a temperature higher than 25 [° C.] of room temperature, that is, by heating the hydrous ethanol used for the extract extraction and using the hot hydrous ethanol, both the extract yield and the polyphenol yield are increased. It was done.

It is a figure which shows the extraction process of the moss extract in this Embodiment, and the manufacturing process of a moss extract product. It is a figure which shows the fundamental measuring method of a bulk density. (A) SEM image of finely pulverized product obtained when supply flow rate is 5.0 [kg / Hr], (b) Finely pulverized product obtained when supply flow rate is 3.5 [kg / Hr] It is a SEM image of. (A) SEM image of finely pulverized product obtained when supply flow rate is 2.5 [kg / Hr], (b) Finely pulverized product obtained when supply flow rate is 1.5 [kg / Hr] It is a SEM image of. It is a SEM image of the finely pulverized material obtained when a supply flow rate is 0.5 [kg / Hr]. The result of Example 1 is shown and it is a figure which shows the relationship between a bulk density and an extract yield. The result of Example 2 is shown and it is a figure which shows the relationship between ethanol concentration and an extract yield. The result of Example 3 is shown, (a) is a figure which shows the relationship between ethanol concentration and the amount of extraction of Ganoderic Alcohol, (b) is the relationship between the ethanol concentration and the amount of extraction of Ganoderic Acid. The result of Example 4 is shown and it is a figure which shows the relationship between ethanol concentration and polyphenol extraction amount. The result of Example 5 is shown and it is a figure which shows the relationship between extraction temperature, an extract yield, and the amount of polyphenols.

Explanation of symbols

  10 ... Finely pulverized product

Claims (10)

Crushing step of crushing fruit bodies of moss,
An extraction step of extracting a hydrous alcohol-soluble extract with hydrous alcohol having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C.] from the ground product of the crushed fruit body;
Following the extraction step, the water-containing alcohol containing the extract is heated at a boiling point or lower to remove the alcohol,
A method for extracting moss extract, comprising: The method for extracting moss extract according to claim 1, wherein, in the extraction step, the extract is extracted from the pulverized product having a bulk density of 0.2 [g / cm ³ ] or more.   The method for extracting moss extract according to claim 1 or 2, wherein an extract yield in the extraction step is 10% or more.   The method for extracting moss extract according to any one of claims 1 to 3, wherein the amount of polyphenol extracted in the extraction step is 4 [mg / g fruiting body] or more. Crushing step of crushing fruit bodies of moss,
An extraction step of extracting a water-soluble ethanol-soluble extract with water-containing ethanol having an ethanol concentration of 30 to 90 [%] and 30 to 80 [° C.] from the pulverized fruit body,
Following the extraction step, the water-containing ethanol containing the extract is heated at a boiling point or lower, and a removal step of removing ethanol,
A product forming step of powdering the extract and using the obtained powder to form a moss extract product,
A method for producing a moss extract product, comprising: The coconut extract product according to claim 5, wherein in the pulverization step, the fruit body is pulverized until a bulk density of the pulverized substance of the fruit body becomes 0.2 [g / cm ³ ] or more. Manufacturing method. An extract of the moss extracted from a pulverized product obtained by pulverizing a fruit body of moss,
An extract of moss characterized in that the extract yield from the fruiting body is 10 [%] or more and the amount of extracted polyphenol is 4 [mg / g fruiting body] or more.   The moss extract according to claim 7, wherein the amount of Ganoderic Alcohols extracted from the fruiting body is 500 [μg / g fruiting body] or more.   The moss extract according to claim 7 or 8, which is extracted from the pulverized product with a hydrous alcohol having an alcohol concentration of 30 to 90 [%] and 30 to 80 [° C]. Extract of the moss extract from the pulverized product obtained by pulverizing the fruit body of moss, and a moss extract product produced using the extracted extract as a raw material,
A moss extract product characterized in that the extract obtained by extraction from the pulverized material with hydrous ethanol having an ethanol concentration of 30 to 90 [%] and 30 to 80 [° C] is used as the raw material.

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