WO2019167325A1 - Extract soluble in physiologically acceptable liquid medium or extracted using physiologically acceptable liquid medium as extraction medium, and method for producing same - Google Patents
Extract soluble in physiologically acceptable liquid medium or extracted using physiologically acceptable liquid medium as extraction medium, and method for producing same Download PDFInfo
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- WO2019167325A1 WO2019167325A1 PCT/JP2018/037707 JP2018037707W WO2019167325A1 WO 2019167325 A1 WO2019167325 A1 WO 2019167325A1 JP 2018037707 W JP2018037707 W JP 2018037707W WO 2019167325 A1 WO2019167325 A1 WO 2019167325A1
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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
- A23L17/00—Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
- A23L17/20—Fish extracts
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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
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
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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
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/17—Amino acids, peptides or proteins
- A23L33/18—Peptides; Protein hydrolysates
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K35/00—Medicinal preparations containing materials or reaction products thereof with undetermined constitution
- A61K35/56—Materials from animals other than mammals
- A61K35/60—Fish, e.g. seahorses; Fish eggs
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K38/00—Medicinal preparations containing peptides
- A61K38/04—Peptides having up to 20 amino acids in a fully defined sequence; Derivatives thereof
- A61K38/05—Dipeptides
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P3/00—Drugs for disorders of the metabolism
- A61P3/02—Nutrients, e.g. vitamins, minerals
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P39/00—General protective or antinoxious agents
- A61P39/06—Free radical scavengers or antioxidants
Definitions
- the present invention relates to an extract that is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium, and a method for producing the same.
- One representative of such foods is marine products represented by fish. Humans have been eating fish for a long time, and features such as high-quality animal protein, low calories, and improvement in brain function have been attracting attention.
- Non-Patent Document 1 In recent years, among fish products that are said to enhance human physiological functions, attention has been focused on fish that focus on antioxidant and / or anti-fatigue effects (Non-Patent Document 1).
- anserine and carnosine are mainly contained in fish.
- high-speed migratory fish such as skipjack and tuna are known to contain a relatively large amount of anserine.
- Carnosine and anserine are also abundantly contained in, for example, pork or chicken in addition to seafood. Therefore, research on carnosine and anserine has been actively promoted.
- carnosine is degraded by carnosine dipeptidase present in serum or tissue, resulting in an obstacle to the function of carnosine. Therefore, a composition for inhibiting carnosine dipeptidase is disclosed (Patent Document 1). ).
- barenin has antioxidant and / or anti-fatigue effects compared to other imidazole dipeptides (carnosine, anserine) from the nature of whales that can continue to swim for long distances without eating food. It is a substance considered to be superior in terms of Therefore, even in situations where whaling is substantially prohibited, it is extremely important for a society that seeks to maintain or improve health to continue to find ways to continuously take imidazole dipeptides, especially valenin. It is.
- the present invention relates to an extract which is rich in imidazole dipeptides, particularly valenine, which is soluble in a physiologically acceptable liquid medium or is extracted using a physiologically acceptable liquid medium as an extraction medium, and a method for producing the same This greatly contributes to the realization of.
- the present inventor In light of the situation where whale meat is virtually incapable or difficult to ingest, the present inventor has conducted research and analysis on marine organisms that may contain valein instead of whales or more than whales, including their ecology. Worked on. As a result of many investigations and analyses, the present inventor has departed from the viewpoint of migratory fish that can respond to continuous exercise, and may have exerted antioxidant and / or anti-fatigue effects in the body due to some influence. I came to focus on the probable deep-sea fish.
- red sea cucumber also called “Mandai”
- valenin a very abundant amount of imidazole dipeptide, especially valenin.
- the present inventor conducted intensive research and analysis of the red squirrel. As a result, for example, even when heat was applied to almost all parts of the red sea cucumber, a very interesting technical finding was obtained that the content of valerine contained in the fish meat does not vary substantially.
- the imidazole dipeptide contained in red squirrel has the following characteristics (1) to (4).
- the part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
- the amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
- the present invention was created based on the above-mentioned viewpoints and technical knowledge.
- One extract of the present invention is an extract which is derived from red squirrel and is extracted using a liquid medium that is soluble or physiologically acceptable in a physiologically acceptable liquid medium.
- this extract contains an imidazole dipeptide, particularly a very abundant amount of valenin, for example, an antioxidative action and / or an anti-fatigue action can be exhibited by ingesting the extract.
- this extract rich in barenin in addition to the above-described action, an effect of suppressing a decrease in muscle activity caused by a decrease in pH due to lactic acid can be exhibited.
- One method of producing an extract according to the present invention is to extract an extract soluble in a physiologically acceptable liquid medium or a physiologically acceptable liquid by bringing the red squirrel into contact with an extraction medium at 20 ° C. or higher.
- An extraction step of extracting an extract extracted using the medium as an extraction medium is included.
- another method for producing an extract of the present invention is to extract an extract that is soluble in a physiologically acceptable liquid medium or physiologically acceptable by bringing the red bowfish into contact with an extraction medium at 60 ° C. or higher.
- imidazole dipeptides in particular extracts that are soluble in physiologically acceptable liquid media containing very abundant amounts of valenin, or physiologically acceptable liquids.
- An extract can be produced that is extracted using the medium as the extraction medium. Therefore, by taking the extract, for example, an antioxidant action and / or an anti-fatigue action can be exhibited.
- contacting redfish (including a cut state or a fragmented state) with a physiologically acceptable liquid medium at 20 ° C. or higher or 60 ° C. or higher Along with coagulation of the protein of the red squirrel, the protein releases the extract that has been retained, so that more accurate recovery of the extract is possible.
- the produced extract can exhibit an effect of suppressing a decrease in muscle activity caused by a decrease in pH due to lactic acid, in addition to the above-described action.
- the extract of the extract that is soluble in a physiologically acceptable liquid medium derived from red sea bream and is extracted using a physiologically acceptable liquid medium as an extraction medium.
- the fact that the ratio is suppressed to less than 5 wt% suppresses variation in the content of imidazole dipeptide or valenin contained in the extract derived from red pepper, in other words, the uniformity of the content of imidazole dipeptide or valenin. From the viewpoint of enhancing, this is a preferred embodiment.
- skin or “skin” means a part having a thickness of less than 10 mm from the outermost surface of the red sea bream toward the inside (inside the body).
- blood meat refers to a portion that exhibits a dark red color among muscles on the body side of fish. If it sees by another parameter
- the extract which is soluble in one physiologically acceptable liquid medium of the present invention or is extracted using a physiologically acceptable liquid medium as an extraction medium, imidazole dipeptides, in particular, very abundant quantities Therefore, by ingesting the extract, for example, it can exhibit an antioxidant effect and / or an anti-fatigue effect.
- 5 is a graph showing the ratio of the amount of barenine extracted using 20 ° C. to 50 ° C. water, where the amount of extracted ballenin is 1.
- an extract which is soluble in a physiologically acceptable liquid medium derived from red sea cucumber or is extracted using a physiologically acceptable liquid medium as an extraction medium and a method for producing the same are attached. This will be described in detail with reference to the drawings.
- FIG. 1 shows an extract (in this embodiment, which is soluble in a physiologically acceptable liquid medium derived from red sea cucumber of this embodiment or extracted using a physiologically acceptable liquid medium as an extraction medium.
- This is a flow showing the manufacturing process of “water-soluble extract.”
- water-soluble extract it is represented as “water-soluble extract” as a representative.
- each processing step shown in FIG. 1 can be all or part of the steps in the method for producing a water-soluble extract. Therefore, the manufacturing method of the water-soluble extract of this embodiment does not necessarily include all the processing steps shown in FIG.
- FIG. 2 is a photograph showing a part of the red bowfish 100 showing the cut part and the site of the red bowfish 100 of the present embodiment.
- the caught red sea bream 100 is frozen (step S1).
- the head 10, muscle 20 normally muscle 20 a and blood 20 b
- the internal organs 30, and the tail fin 90 of the red sea bream 100 are separated, respectively.
- a cutting (disassembling) step of cutting the frozen red sea bream 100 along C 1 , C 2 , and C 3 in a substantially straight line is performed (step S2).
- part including a back fin does not appear in a photograph, since the site
- cutting as shown in C 1 in FIG. 2 as sickle of red sunfish 100 of the present embodiment is not included in the muscle 20, and along a substantially tangential direction of the end portion of the muscle 20 side of the hook To be implemented.
- the cutting shown in C 2 in FIG. 2 the eyes and mouth of the red sunfish 100 of the present embodiment is performed as included in the head 10.
- the cutting shown in C 3 the muscles 20 of red sunfish 100 of this embodiment is carried out as much as possible, not included in the tail fin 90.
- the tail fin 90 is not a raw material for the water-soluble extract of the present embodiment, and thus the description of the part is omitted.
- a known band saw device is used, but means for cutting the red bowfish in the step is not limited to the band saw device.
- Other known cutting methods that can cut frozen red sea cucumbers along C 1 , C 2 , and C 3 may also be employed.
- a known chopper device for example, model: MC-22, manufactured by NANTUNE Co., Ltd.
- a known chopper device for example, model: MC-22, manufactured by NANTUNE Co., Ltd.
- Each part (head 10, normal muscle 20a, blood joint meat 20b, internal organs 30, skin 40) of red sea bream 100 is thawed completely or incompletely.
- a fragmentation step using the chopper device for example, each of the minced portions that are fragmented from a plate having a through hole of 10 mm ⁇ can be obtained.
- a known chopper device is used.
- means for obtaining the respective parts that are stripped in the step are not limited to the chopper device.
- a known silent cutter can also be employed in the fragmentation process.
- Table 1 “Bal.” Means “valenin content”. “Ans.” Means “anserine content” and “Cal.” Means “carnosine content”. Therefore, “total (Imd.)” In Table 1 means the content of imidazole dipeptide. In order to facilitate understanding, the lower part of each numerical value displays the ratio (%) to the content of imidazole dipeptide in parentheses. In addition, after “ ⁇ ” in each column in Table 1, it means standard deviation. Further, the skin part 40 as the analysis target in Table 1 is a skin of the site of the muscle 20. In addition, the value of the first place in each numerical value in Table 1 and Table 2 described later is rounded off.
- the presence of valenin was clarified based on the result of detection of high concentrations of 3-methylhistidine by analyzing the bound amino acids by hydrolysis with hydrochloric acid.
- the amount of valerin in each segmented portion was quantified.
- this analysis revealed the following characteristics (1) to (4) regarding the amount of imidazole dipeptide containing valerin in each segmented portion.
- the part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
- the amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
- each segmented portion head 10, normal muscle 20 a, blood meat 20 b, internal organ 30, skin part derived from red sea bream 100
- the amount of barenine contained in 40 is equivalent to or much larger than the amount of barenine contained in the minced whale red meat.
- the content of valenin from the center of the normal muscle 20a to the head side normal muscle 20a and the content of imidazole dipeptide are the same as the normal muscle 20a from the center of the normal muscle 20a. It was confirmed that the content of valenin of 20a and the content of imidazole dipeptide were about 10% higher.
- the position of the “center of the normal muscle 20a” is the length from the tip of the head 10 (tip of the mouth) to the tail-side end of the normal muscle 20a (and thus not including the tail fin 90). This is defined as a position of 0.5 from the front end when “L” in FIG. 2 is 1. Therefore, in order to obtain the normal muscle 20a having a high content of valenin with higher accuracy, it is preferable to obtain imidazole dipeptide and / or valenin from the normal muscle 20a including the normal muscle 20a from the head side tip to 0.4 or less. This is one aspect.
- each segmented portion is then brought into contact with water (ion exchange water) as an extraction medium at about 60 to about 100 ° C. More specifically, an extraction step (step S3) is performed in which each segmented portion is immersed in the extraction medium at about 60 ° C. to about 100 ° C. in a known container.
- stirring of this extraction medium is not performed intentionally, stirring this extraction medium intentionally is also one aspect
- a separation process is performed in which the aqueous solution is separated from the respective parts (which can be handled as a residue) using a centrifuge (step S4).
- the water-soluble extract of this embodiment can be produced by performing centrifugal filtration using a 300-mesh filter cloth.
- the water-soluble extract of this embodiment is liquid.
- centrifugal filtration using a 300 mesh filter cloth is employed, but the separation process of the present embodiment is not limited to such a mode.
- a known separation step for example, separation treatment by centrifugal sedimentation
- ⁇ Modification Example (1) of First Embodiment> by further concentrating the water-soluble extract produced by the water-soluble extract production process of the first embodiment, a more abundant amount of imidazole dipeptide or valenin A concentration step (step S5) for producing a water-soluble extract (hereinafter also simply referred to as “concentrated extract”) as a concentrated extract containing sucrose may be performed.
- a water-soluble extract hereinafter also simply referred to as “concentrated extract”
- the water-soluble extract of the first embodiment is stirred or allowed to stand in a space of about 60 ° C. for about 1 hour to about 8 hours and at a reduced pressure (eg, 0.03 MPa).
- a concentrated extract can be produced.
- the concentration process of this modification is not limited to such an embodiment.
- the concentration step (step S5) if the temperature at which the water-soluble extract of the first embodiment is stirred or allowed to stand is 20 ° C or higher, 30 ° C or higher, 40 ° C or higher, or 50 ° C or higher, At least some of the effects of the modification can be achieved.
- the amount of valenin contained in the concentrated extract obtained by the concentration step of this modification for example, it contains about 75 wt% of water (in other words, the solid content is about 25 wt%).
- the concentrated extract was used as a sample, it was confirmed that the content of valerin relative to the total amount of the concentrated extract was 5 wt% or more (more narrowly, 9 wt% or more). Therefore, it has been clarified that the amount of imidazole dipeptide contained in the concentrated extract obtained by the concentration step of this modification is also contained in an amount of 5 wt% or more (more narrowly, 9 wt% or more).
- a soluble or physiologically acceptable liquid that is soluble in a physiologically acceptable liquid medium as the concentrated extract of the modification (1) of the first embodiment Manufactured by a manufacturing process of an extract that is extracted using a medium as an extraction medium (in this variation, “water-soluble extract”. Hereinafter, in this variation, it is represented as “water-soluble extract” as a representative).
- the drying process step S6 which obtains a dry extract by drying the concentrated extract made can be performed.
- a vacuum drying (including reduced pressure drying) process or a freeze drying process is performed as a typical example of the drying process.
- the “vacuum drying (or reduced pressure drying) step” in this modification means a step of drying in a vacuum state (or reduced pressure state) while heating.
- the “freeze-drying step” in the present modification includes a “freeze-vacuum drying step” or a “freeze-decompression drying step”.
- hot air drying is used instead of the above two types of drying steps. It is also possible to employ a drying process by microwave drying, superheated steam drying, fly drying, reduced-pressure fly drying, drum drying, or sun drying.
- a vacuum drying process when a vacuum drying process is employed, a known method and apparatus can be used. For example, a continuous belt dryer or a vacuum drum dryer may be employed.
- a modification (1) of the first embodiment is performed for about 12 hours to about 72 hours in an environment of about 60 ° C. under a gauge pressure of ⁇ 0.093 MPa with the atmospheric pressure being 0.
- the dried extract of this modification can be formed by stirring or leaving the concentrated extract of).
- the temperature at which the concentrated extract of the modified example (1) of the first embodiment is stirred or allowed to stand is 20 ° C or higher, 30 ° C or higher, 40 ° C or higher, or 50 ° C or higher.
- at least a part of the effects of the present modification can be achieved.
- a freeze-drying apparatus Kyowa Vacuum Technology Co., Ltd., model: RL4522BS
- the concentrated extract of the modified example (1) of the first embodiment is stirred or allowed to stand for about 168 hours under a pressure of about 266 Pa and in an environment of about ⁇ 20 ° C.
- the dry extraction of this modification containing 7 wt% (more narrowly, 10 wt% or more, 15 wt% or more, or 20 wt% or more, more narrowly defined 25 wt% or more, very narrowly defined 30 wt% or more) Things can be formed.
- the moisture content of the dried extract of the present modification represented by vacuum drying or freeze drying can be adjusted as appropriate by known means. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the moisture content is more than 0 wt% and not more than 10 wt% of the dry extract of this modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the dry extract of the present modification, and further preferably 3 wt% or less of the dry extract of the present modification.
- a powdering step (step S7) for obtaining a coarse powder by further crushing the dried extract of the present modification is performed.
- a powdering step for example, a known hammer mill (for example, a hammer mill manufactured by Hosokawa Micron Corporation) may be employed. More specifically, the dry extract of this modification can be pulverized under the processing conditions set so that the particle size is 2 mm or less.
- a dry extract (hereinafter, also simply referred to as “coarse powder”) as the coarse powder of the present embodiment, which is derived from the red pepper 100, can be produced.
- the present inventor analyzed the amount of valenin contained in the dry extract as a coarse powder obtained by the powdering step of the present modification.
- a coarse powder containing about 5 wt% water in other words, having a solid content of about 95 wt%) is used as a sample
- the coarse powder The content of valerine with respect to the total amount of the material is 7 wt% (10 wt% or more in the narrow sense, or 15 wt% or more, or 20 wt% or more, 25 wt% or more in the narrow sense, 30 wt% or more in the very narrow sense). It was confirmed that the content was high.
- the amount of imidazole dipeptide contained in the coarse powder obtained by the powdering step of this modification is also 7 wt% (more narrowly 10 wt% or more, 15 wt% or more, or 20 wt% or more, and more narrowly, 25 wt% or more, and in a very narrow sense, 30 wt% or more) was revealed.
- the moisture content of the dried extract as the coarse powder of the present modification can be adjusted as appropriate by known means, as described above. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the water content is more than 0 wt% and not more than 10 wt% of the coarse powder of this modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the coarse powder of the present modification, and further preferably 3 wt% or less of the coarse powder of the present modification.
- the coarse powder of this modified example is a coarse powder produced without undergoing a purification process. More specifically, the coarse powder is prepared by dissolving the coarse powder in water or the like, as in the method disclosed in Non-Patent Document 2, for example, and then using an ion exchange resin (for example, cation exchange).
- a crude powder obtained without performing a step of extracting and purifying imidazole dipeptide containing valenin using a resin Therefore, even if the crude powder is not purified, it contains, for example, an imidazole dipeptide capable of exerting an antioxidant action and / or an anti-fatigue action, in particular, a very abundant amount of valenin as described above. Is worthy of note because it produces many advantages such as improving yield (including yield) of imidazole dipeptide and / or valenin, simplifying manufacturing process (including shortening manufacturing time), and reducing manufacturing cost. .
- the dried extract as a coarse powder produced by the production process of the modified example (2) of the first embodiment is further classified to be less than 1 mm (more Preferably, a classification step (step S8) for obtaining a dry extract (hereinafter also simply referred to as “fine powder”) as a fine powder composed of a powder having a particle diameter of less than 0.8 mm) may be performed.
- step S8 of this modification for example, only fine powder that passes through a sieve having a sieve opening of 0.7 mm can be collected.
- the dry extract of the present modification derived from the red squirrel 100 (the dry extract as a fine powder composed of a powder having a particle diameter of less than 1 mm).
- adopted in the powdering process in the modification (2) of 1st Embodiment are also provided with the classification function, a powdering process and a classification process can be implemented simultaneously.
- the present inventor analyzed the amount of barenin contained in the fine powder obtained by the classification process of this modification.
- the total amount of fine powder is 7 wt% (10 wt% or more in a narrow sense, 15 wt% or more, or 20 wt% or more, 25 wt% or more in a narrow sense, 30 wt% or more in a very narrow sense) The amount was confirmed.
- the amount of imidazole dipeptide contained in the fine powder obtained by the classification step of this modification is also 7 wt% (more narrowly 10 wt% or more, 15 wt% or more, or 20 wt% or more, and more narrowly 25 wt%). As described above, it was revealed that 30 wt% or more is contained in a very narrow sense. In addition, to describe the highest result that the present inventors have confirmed at this stage, the value of about 35 wt% is obtained as the content of only barenin relative to the total amount of the dry extract as a fine powder. Deserves special mention.
- the fine powder of this modification is evaluated from another viewpoint, for example, when focusing on the muscle 20 of the red sea bream 100, when the mass (for example, 1 kg) of the captured muscle 20 of the red sea bream 100 is used as a reference
- the mass ratio (ie, yield) of the dry extract derived from the muscle 20 was more than 50 g (60 g or more in a narrow sense).
- an example of the proportion of the content of valerin in the dry extract as a fine powder was an extremely high value of 25 wt% or more (more narrowly, 30 wt% or more).
- the moisture content of the dry extract as the fine powder of the present modification can be adjusted as appropriate by known means, as described above. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the water content is more than 0 wt% and not more than 10 wt% of the fine powder of the present modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the fine powder of the present modification, and further preferably 3 wt% or less of the fine powder of the present modification.
- the dry extract as a fine powder in the present modification is a fine powder produced without undergoing a purification process. More specifically, the fine powder is obtained by dissolving the fine powder in water or the like, as in the method disclosed in Non-Patent Document 2, for example, and then an ion exchange resin (for example, a cation exchange resin). Is a fine powder obtained without performing the step of extracting and purifying imidazole dipeptide containing valenin. Therefore, even a fine powder as an unpurified fine powder contains, for example, an imidazole dipeptide capable of exerting an antioxidant action and / or an anti-fatigue action, in particular, a very abundant amount of valenin. Deserves special mention.
- Table 2 shows a soluble or physiologically acceptable liquid in a physiologically acceptable liquid medium of the normal muscle 20a when each process (steps S1 to S8) from the freezing process to the classification process is performed.
- Table 1 of extracts extracted using the medium as an extraction medium in this variation, “water-soluble extract”.
- water-soluble extract it is represented as “water-soluble extract” as a representative).
- An example of the analysis result is shown.
- the presence of valenin was clarified based on the result of detection of a high concentration of 3-methylhistidine by analyzing the bound amino acid by hydrolysis with hydrochloric acid. Further, the amount of barenin in the water-soluble extract at each site was quantified by quantifying the amount of barenin based on 3-methylhistidine in the hydrolyzed extract using a standard product of barenine.
- the content of imidazole dipeptide (including valenin) in the water-soluble extract produced from the normal muscle 20a cut by step S2 of the first embodiment (for example, 27850 mg / day in Table 2)
- the ratio of the valenine content (for example, 23870 mg / 100 g in Table 2) to 100 g) was about 86%. This value can be said to be almost equivalent to the ratio (about 88%) of the same standard in Table 1.
- the above ratio is also referred to as “imidazole dipeptide-valenine ratio”.
- the water-soluble extract produced in this embodiment can achieve an extremely high valenine content and an extremely high “imidazole dipeptide-valenine ratio”.
- the water-soluble extract produced in the present embodiment has the imidazole dipeptide content, the valenin content, and the aforementioned “imidazole dipeptide-valenine ratio” at each site derived from the red sea cucumber of the first embodiment, It was confirmed that the substance can be reflected almost as it is.
- the amount of barenin contained in the water-soluble extract produced in the present embodiment is equal to the amount of ballenin contained in the minced whale back meat red meat, or It can be said that it is much more than the amount.
- the content of valenin contained in the water-soluble extract produced in the present embodiment the content of imidazole dipeptide, and “ Regarding the “imidazole dipeptide-valenine ratio”, the present inventors have found that the following numerical range can be realized.
- the content of valenin is 7 wt% or more (more narrowly, 10 wt% or more) based on the total mass of the water-soluble extract.
- the content of imidazole dipeptide is 25 wt% or more with respect to the mass of the entire water-soluble extract.
- step S1 to S6 from the freezing step to the drying step (steps S1 to S6) shown in the first embodiment and the modifications (1) to (2) thereof, the freezing step to the pulverization are performed.
- steps S1 to S7 After each process up to the process (steps S1 to S7), each process from the freezing process to the classification process (not shown) (steps S1 to S8), or after the freezing process is separated (steps S1 to S4)
- the purification process step S9 of this embodiment is performed.
- step S9 of the present embodiment after the dry extract or the dry extract as a coarse powder is dissolved in water or the like as in the method disclosed in Non-Patent Document 2, ion exchange is performed. Using a resin (for example, a cation exchange resin), a step of extracting and purifying imidazole dipeptide containing valenin is performed. As a result, it is possible to produce a water-soluble extract containing an imidazole dipeptide having a richer content than in the first embodiment and its modifications (1) to (3) and a rich content of valenin. .
- a resin for example, a cation exchange resin
- the upper limit of the content of imidazole dipeptide and the content of valenin with respect to the total mass of the water-soluble extract obtained by performing the purification step (step S9) of this embodiment is not particularly limited, It can be said that the upper limit is less than 100 wt%. If the upper limit is dared to be mentioned, the content of the imidazole dipeptide and the content of the valenine are 99 wt% or less in a narrower sense, and 95 wt% or less in a narrower sense. The numerical range of the upper limit value can be applied to other embodiments.
- part the head 10, the normal muscle 20a, the blood muscle 20b, the internal organs 30, and the skin part 40 of the red sea bream 100.
- the process (step S8) or the purification process (step S9) is performed, the present embodiment is not limited to such an aspect.
- step S2 in order to be able to mix the visceral part 30 and the skin part 40 with a large amount of imidazole dipeptide because they contain a lot of carnosine, the cutting (disassembly) step (step S2) and subsequent steps are performed. It is also an embodiment that can adopt each step. In addition, it is possible to mix all the parts (head 10, normal muscle 20a, blood meat 20b, internal organs 30, skin 40) having distinctive features of being rich in imidazole dipeptides containing valenine; It is one mode which can also adopt that each process after a cutting (disassembly) process (Step S2) is carried out so that it may become.
- the red sea bream caught by the longline fishing boat is quickly frozen (for example, within 60 minutes) on the fishing boat at a low temperature freezing treatment
- a low temperature freezing treatment for example, the method for catching red sea bream and the method for storing red sea bream in a fishing boat are not limited to the above examples.
- the captured red squirrel is quickly (eg, within 60 minutes) on a fishing boat.
- a low-temperature freezing treatment for example, ⁇ 65 ° C. or more and ⁇ 15 ° C. or less) is a preferable embodiment.
- the extraction step in which each portion of the striped red sea bream 100 is immersed in an extraction medium (for example, water) of about 60 ° C. or more and about 100 ° C. or less in the container.
- Step S3 is performed, but the first embodiment is not limited to such an extraction process.
- adopting an extraction process (step S3) as shown in the following (a) to (c) is also a preferred modification of the first embodiment.
- the pressure in the container of the extraction step is different from the normally employed about 1 atm (about 0.101 MPa) (for example, about 0.001 MPa to about 100 MPa (excluding about 0.101 MPa))
- the aforementioned “physiologically acceptable liquid medium” is not limited to alcohol (typically, high-purity ethanol (eg, 99.5% or 100%)).
- it can include beer, wine, and brewed liquors including sake, whiskey, shochu, and distilled liquor including vodka, and mixed liquor including cassis and campari. Needless to say, water is included in the “physiologically acceptable liquid medium”.
- step S3 As a modification of the first embodiment described above, when the extraction step (a) is adopted, extraction at a lower temperature is realized, thus saving energy. Can contribute.
- the temperature of the extraction medium is 20 ° C. under a normally employed about 1 atm (about 0.101 MPa)
- the temperature as an example of the first embodiment about 60 ° C. In this case, it has been found that about 0.77 can be extracted when the amount that can be extracted is 1).
- FIG. 4 shows the amount of barenine in the normal muscle 20a (mg / 100 g) (dotted line in FIG. 4) when extracted using water having a temperature of 20 ° C. to 60 ° C. in the extraction step of the first embodiment.
- FIG. 4 is a graph showing the ratio of the amount of valenine extracted using water at 20 ° C. to 50 ° C. when the amount of valenine extracted using water at a temperature of 60 ° C. is 1 (solid line in FIG. 4). It is.
- the method for analyzing the amount of valenin is the same as the method described in the first embodiment.
- the extraction process of (c) when the extraction process of (c) is employ
- the amount of imidazole dipeptide (typically valenin) when the extraction step (c) described above is performed using ethanol (purity 99.5%) is the imidazole when water is used as the extraction medium. It has been confirmed to be about 70% of the amount of dipeptide (typically valenin).
- the extraction medium is alcohol
- the extraction amount is reduced compared to when the extraction medium is water, but even if it is about 70% of the extraction amount in the case of water, a considerable amount of imidazole dipeptide (typically It is worth mentioning that valenin is extracted. Therefore, even when an extraction medium other than water is employed, at least some of the effects of the first embodiment can be achieved.
- the dorsal fin or tail fin 90 of the red sea bream 100 is a physiologically acceptable liquid. Extracts extracted using a medium soluble or physiologically acceptable liquid medium as an extraction medium (typically a water-soluble extract, but not limited to a water-soluble extract.
- the extract is not limited to such an embodiment, although it is not included in the following.
- the dorsal fin and / or tail fin 90 is included as one of the constituent components of the extract of the first embodiment and its modifications (1) to (3) and the second embodiment. obtain.
- the amount of imidazole dipeptide or valenin contained in the blood meat 20b varies greatly. Therefore, it can be said from the viewpoint of obtaining an extract which contains a more stable amount of imidazole dipeptide or valenine and is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium.
- the amount of the mixed blood 20b to be mixed is preferably less than 5 wt%.
- the first embodiment and its modifications (1) to (3) and the extract of the second embodiment are derived from red sea cucumber and formed from bloody meat.
- compositions are soluble or physiological in a physiologically acceptable liquid medium manufactured in the first embodiment and its modifications (1) to (3), the second embodiment, and other embodiments.
- Producing agents, drops, chickenpox and the like (hereinafter collectively referred to as “formulations”) is a preferred embodiment that can be employed.
- the preparation contains an imidazole dipeptide, in particular, a very abundant amount of valenin, for example, an antioxidant action and / or an anti-fatigue action can be achieved by taking the preparation.
- this formulation can be manufactured by a well-known manufacturing method.
- the preparation may be mixed with excipients, binders, disintegrants, wetting agents, honey or rice flour, etc., as appropriate, in order to improve moldability or ease of oral administration. Can be formed.
- the extract which is soluble in one physiologically acceptable liquid medium of the present invention or is extracted using a physiologically acceptable liquid medium as an extraction medium, a method for producing the same, and a dosage form are rich in valenin. Since it is the fish-derived extract obtained and the method for producing the same, it is extremely useful not only in the food industry and the fishery industry but also in various industries related to medicine, health, medical care, and beauty.
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Abstract
One of the extracts of the present invention, which is soluble in a physiologically acceptable liquid medium or extracted using, as an extraction medium, a physiologically acceptable liquid medium, is derived from Lampris guttatus 100. This extract contains imidazole dipeptides, in particular extremely high levels of Balenine. Therefore, taking this extract may result in an antioxidant action and/or an antifatigue action, for example.
Description
本発明は、生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法に関する。
The present invention relates to an extract that is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium, and a method for producing the same.
健康は市民生活を豊かにし、活力ある社会の構築に貢献する。健康の維持又は増進に役立ち得る食品を提供することは、今や先進国のみならず開発途上国においても重要な課題である。そのような食品の代表格の一つは、魚に代表される水産物である。人間は、長期にわたって魚を食しており、その良質な動物性たんぱく質、低カロリー、及び脳機能の改善といった特徴については、従来から注目されてきた。
“Health enriches citizens' lives and contributes to the creation of a vibrant society. Providing foods that can help maintain or enhance health is now an important challenge not only in developed countries but also in developing countries. One representative of such foods is marine products represented by fish. Humans have been eating fish for a long time, and features such as high-quality animal protein, low calories, and improvement in brain function have been attracting attention.
近年、人間の生理機能を高めると言われる水産物のうち、抗酸化作用及び/又は抗疲労作用等に着目した魚にも注目が集まっている(非特許文献1)。
In recent years, among fish products that are said to enhance human physiological functions, attention has been focused on fish that focus on antioxidant and / or anti-fatigue effects (Non-Patent Document 1).
例えば、イミダゾールジペプチドに分類される物質が主として3種類が存在し、一般的には、魚の中に存在するイミダゾールジペプチドの種類は偏っている。具体的には、イミダゾールジペプチドのうち、アンセリンとカルノシンが主として魚に含まれている。例えば、カツオ、マグロといった高速回遊魚は、アンセリンを比較的多く含むことが知られている。また、カルノシンとアンセリンは、魚介類以外にも、例えば豚肉又は鶏肉に豊富に含まれている。そのため、カルノシンとアンセリンについての研究は盛んに進められている。特にカルノシンについては、血清又は組織中に存在するカルノシンジペプチダーゼによってカルノシンが分解され、カルノシンの機能発揮の障害となっていることから、カルノシンジペプチダーゼ阻害用組成物が開示されている(特許文献1)。
For example, there are mainly three types of substances classified as imidazole dipeptides, and in general, the types of imidazole dipeptides present in fish are biased. Specifically, among imidazole dipeptides, anserine and carnosine are mainly contained in fish. For example, high-speed migratory fish such as skipjack and tuna are known to contain a relatively large amount of anserine. Carnosine and anserine are also abundantly contained in, for example, pork or chicken in addition to seafood. Therefore, research on carnosine and anserine has been actively promoted. In particular, for carnosine, carnosine is degraded by carnosine dipeptidase present in serum or tissue, resulting in an obstacle to the function of carnosine. Therefore, a composition for inhibiting carnosine dipeptidase is disclosed (Patent Document 1). ).
一方、イミダゾールジペプチドに分類される他の物質は、バレニンである。バレニンを筋肉等に含む動物は、鯨やホタテガイ等、極めて限定されている。加えて、他のイミダゾールジペプチドとともにバレニンを比較的多く含む肉として知られている鯨肉は、捕鯨が実質的に禁止されている状況では、摂取することが不可能又は非常に困難となっている。そのため、かつて捕鯨国であった国であっても、現状ではバレニンを摂取する機会が非常に少なくなっている。
On the other hand, another substance classified as imidazole dipeptide is barenin. Animals that contain ballenin in their muscles are extremely limited, such as whales and scallops. In addition, whale meat, known as meat with a relatively high amount of ballenin along with other imidazole dipeptides, is impossible or very difficult to consume in situations where whaling is substantially prohibited . As a result, even in countries that used to be whaling countries, there are now very few opportunities for taking valenin.
イミダゾールジペプチドの中でも、バレニンは、餌も食べずに長距離を泳ぎ続けることができる鯨の生態からも、他のイミダゾールジペプチド(カルノシン、アンセリン)と比較して、抗酸化作用及び/又は抗疲労作用の観点で優位性があると考えられる物質である。従って、捕鯨が実質的に禁止されている状況であっても、イミダゾールジペプチド、特にバレニンを継続的に摂取するための方法を見出す努力を続けることは、健康の維持又は増進を図る社会にとって極めて重要である。
Among imidazole dipeptides, barenin has antioxidant and / or anti-fatigue effects compared to other imidazole dipeptides (carnosine, anserine) from the nature of whales that can continue to swim for long distances without eating food. It is a substance considered to be superior in terms of Therefore, even in situations where whaling is substantially prohibited, it is extremely important for a society that seeks to maintain or improve health to continue to find ways to continuously take imidazole dipeptides, especially valenin. It is.
本発明は、イミダゾールジペプチド、特にバレニンを豊富に含み得る、生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法の実現に大きく貢献するものである。
The present invention relates to an extract which is rich in imidazole dipeptides, particularly valenine, which is soluble in a physiologically acceptable liquid medium or is extracted using a physiologically acceptable liquid medium as an extraction medium, and a method for producing the same This greatly contributes to the realization of.
本発明者は、鯨肉が実質的に摂取不可能又は困難となった状況を踏まえ、鯨に代わる、又は鯨を超えるバレニンを含む可能性のある海洋生物について、その生態を含めた研究と分析に取り組んだ。多くの調査と分析を重ねた結果、本発明者は、連続的運動に対応できる回遊魚という観点から離れ、何らかの影響によって抗酸化作用及び/又は抗疲労作用を体内で発揮しているであろうと思われる深海魚に着眼するに至った。
In light of the situation where whale meat is virtually incapable or difficult to ingest, the present inventor has conducted research and analysis on marine organisms that may contain valein instead of whales or more than whales, including their ecology. Worked on. As a result of many investigations and analyses, the present inventor has departed from the viewpoint of migratory fish that can respond to continuous exercise, and may have exerted antioxidant and / or anti-fatigue effects in the body due to some influence. I came to focus on the probable deep-sea fish.
その後の本発明者による更なる試行錯誤と分析により、様々な深海魚の中でもアカマンボウ(「マンダイ」とも呼ばれる)が、非常に豊富な量のイミダゾールジペプチド、特にバレニンを含有していることを本発明者は知得した。そこで、本発明者がこのアカマンボウの研究と分析を集中的に行った。その結果、例えばアカマンボウの略全ての部位に対して熱を加えた場合であっても、該魚肉が有するバレニン含有量が実質的に変動しないという、大変興味深い技術的知見を得た。
Subsequent trial and error and analysis by the inventor revealed that among various deep-sea fish, red sea cucumber (also called “Mandai”) contains a very abundant amount of imidazole dipeptide, especially valenin. The person knew. Therefore, the present inventor conducted intensive research and analysis of the red squirrel. As a result, for example, even when heat was applied to almost all parts of the red sea cucumber, a very interesting technical finding was obtained that the content of valerine contained in the fish meat does not vary substantially.
さらに分析を進めたところ、アカマンボウが含有するイミダゾールジペプチドが下記の(1)~(4)の特徴を有することも、本発明者は知得した。
(1)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(頭部、内臓、及び皮)も、可食部(普通筋)に匹敵する量のバレニンを含んでいること。
(2)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(内臓、及び皮)が含有するイミダゾールジペプチドの量は、該可食部(普通筋)が含有するイミダゾールジペプチドの量よりも顕著に多いこと。
(3)アカマンボウの、いわゆる可食部(普通筋)が含有するイミダゾールジペプチドの種類ごとの量と、該可食部(普通筋)と異なる部位(特に、内臓及び皮)が含有するイミダゾールジペプチドの種類ごとの量とが顕著に異なっていること。
(4)アカマンボウの普通筋と比較して、血合肉のイミダゾールジペプチド(バレニンを含む)の量のバラつき(標準偏差)が非常に大きいこと。 As a result of further analysis, the present inventor has also found that the imidazole dipeptide contained in red squirrel has the following characteristics (1) to (4).
(1) The part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
(2) The amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
(3) The amount of each kind of imidazole dipeptide contained in the so-called edible part (ordinary muscle) of red squirrel and the imidazole dipeptide contained in a part (particularly, viscera and skin) different from the edible part (ordinary muscle) The amount of each type is significantly different.
(4) The variation (standard deviation) in the amount of imidazole dipeptide (including valerine) in the blood meat is very large compared to the common muscle of red sea bream.
(1)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(頭部、内臓、及び皮)も、可食部(普通筋)に匹敵する量のバレニンを含んでいること。
(2)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(内臓、及び皮)が含有するイミダゾールジペプチドの量は、該可食部(普通筋)が含有するイミダゾールジペプチドの量よりも顕著に多いこと。
(3)アカマンボウの、いわゆる可食部(普通筋)が含有するイミダゾールジペプチドの種類ごとの量と、該可食部(普通筋)と異なる部位(特に、内臓及び皮)が含有するイミダゾールジペプチドの種類ごとの量とが顕著に異なっていること。
(4)アカマンボウの普通筋と比較して、血合肉のイミダゾールジペプチド(バレニンを含む)の量のバラつき(標準偏差)が非常に大きいこと。 As a result of further analysis, the present inventor has also found that the imidazole dipeptide contained in red squirrel has the following characteristics (1) to (4).
(1) The part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
(2) The amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
(3) The amount of each kind of imidazole dipeptide contained in the so-called edible part (ordinary muscle) of red squirrel and the imidazole dipeptide contained in a part (particularly, viscera and skin) different from the edible part (ordinary muscle) The amount of each type is significantly different.
(4) The variation (standard deviation) in the amount of imidazole dipeptide (including valerine) in the blood meat is very large compared to the common muscle of red sea bream.
本発明は、上述の視点、及び技術的知見に基づいて創出された。
The present invention was created based on the above-mentioned viewpoints and technical knowledge.
本発明の1つの抽出物は、アカマンボウ由来であり、かつ生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物である。
One extract of the present invention is an extract which is derived from red squirrel and is extracted using a liquid medium that is soluble or physiologically acceptable in a physiologically acceptable liquid medium.
この抽出物によれば、イミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有しているため、該抽出物を摂取することにより、例えば抗酸化作用及び/又は抗疲労作用を発揮し得る。なお、バレニンを豊富に含むこの抽出物によれば、上述の作用以外にも、乳酸によるpH低下に起因する筋活動の低下を抑制する効果が奏され得る。
Since this extract contains an imidazole dipeptide, particularly a very abundant amount of valenin, for example, an antioxidative action and / or an anti-fatigue action can be exhibited by ingesting the extract. In addition, according to this extract rich in barenin, in addition to the above-described action, an effect of suppressing a decrease in muscle activity caused by a decrease in pH due to lactic acid can be exhibited.
本発明の1つの抽出物の製造方法は、アカマンボウを20℃以上の抽出媒体に接触させることにより、生理学的に許容可能な液状媒体に可溶な抽出物、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を抽出する、抽出工程を含む。
One method of producing an extract according to the present invention is to extract an extract soluble in a physiologically acceptable liquid medium or a physiologically acceptable liquid by bringing the red squirrel into contact with an extraction medium at 20 ° C. or higher. An extraction step of extracting an extract extracted using the medium as an extraction medium is included.
また、本発明のもう1つの抽出物の製造方法は、アカマンボウを60℃以上の抽出媒体に接触させることにより、生理学的に許容可能な液状媒体に可溶な抽出物、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を抽出する、抽出工程を含む。
Further, another method for producing an extract of the present invention is to extract an extract that is soluble in a physiologically acceptable liquid medium or physiologically acceptable by bringing the red bowfish into contact with an extraction medium at 60 ° C. or higher. An extraction step for extracting an extract that is extracted using a possible liquid medium as an extraction medium;
これらの抽出物の製造方法によれば、イミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有する、生理学的に許容可能な液状媒体に可溶な抽出物、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を製造することができる。そのため、該抽出物を摂取することにより、例えば抗酸化作用及び/又は抗疲労作用を発揮し得る。また、上述の抽出工程においては、20℃以上又は60℃以上の生理学的に許容可能な液状媒体にアカマンボウ(切断された状態、又は細片化された状態を含む)を接触させることは、アカマンボウが有するタンパク質を凝固させるとともに、該タンパク質が、いわば保持していた該抽出物を解放することになるため、該抽出物のより確度高い回収を可能にする。なお、バレニンを豊富に含むこの抽出物を製造することにより、製造された該抽出物は、上述の作用以外にも、乳酸によるpH低下に起因する筋活動の低下を抑制する効果が奏し得る。
According to the method for producing these extracts, imidazole dipeptides, in particular extracts that are soluble in physiologically acceptable liquid media containing very abundant amounts of valenin, or physiologically acceptable liquids. An extract can be produced that is extracted using the medium as the extraction medium. Therefore, by taking the extract, for example, an antioxidant action and / or an anti-fatigue action can be exhibited. Moreover, in the above-described extraction step, contacting redfish (including a cut state or a fragmented state) with a physiologically acceptable liquid medium at 20 ° C. or higher or 60 ° C. or higher, Along with coagulation of the protein of the red squirrel, the protein releases the extract that has been retained, so that more accurate recovery of the extract is possible. In addition, by producing this extract rich in barenin, the produced extract can exhibit an effect of suppressing a decrease in muscle activity caused by a decrease in pH due to lactic acid, in addition to the above-described action.
なお、上述のとおり、該アカマンボウの血合肉が含有するイミダゾールジペプチド(バレニンを含む)の量のバラつきが高いことが明らかとなった。従って、上述の各発明において、血合肉から形成されたアカマンボウ由来の生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物の割合が5wt%未満にまで抑えられることは、該アカマンボウ由来の該抽出物が含有するイミダゾールジペプチド又はバレニンの含有量のバラつきを抑える、換言すれば、イミダゾールジペプチド又はバレニンの含有量の均一性を高める観点から、好適な一態様である。
As described above, it has been clarified that the amount of imidazole dipeptide (including valerine) contained in the red sea bream blood meat is highly variable. Therefore, in each of the above-described inventions, the extract of the extract that is soluble in a physiologically acceptable liquid medium derived from red sea bream and is extracted using a physiologically acceptable liquid medium as an extraction medium. The fact that the ratio is suppressed to less than 5 wt% suppresses variation in the content of imidazole dipeptide or valenin contained in the extract derived from red pepper, in other words, the uniformity of the content of imidazole dipeptide or valenin. From the viewpoint of enhancing, this is a preferred embodiment.
ところで、本願において「皮」又は「皮部」とは、アカマンボウの最表面から内側(体内側)に向けて10mm未満の厚みを有する部位を意味する。また、本願において「血合肉」とは、魚類の体側にある筋肉のうち、暗赤色を呈する部分をいう。別の指標で見れば、本願において「血合肉」とは、「普通筋」に含まれる鉄分量の2倍以上の鉄分量を含有する部位をいう。
By the way, in the present application, “skin” or “skin” means a part having a thickness of less than 10 mm from the outermost surface of the red sea bream toward the inside (inside the body). Further, in the present application, “blood meat” refers to a portion that exhibits a dark red color among muscles on the body side of fish. If it sees by another parameter | index, in this application, "blood meat" means the site | part containing the iron content more than twice of the iron content contained in "normal muscle".
本発明の1つの生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物によれば、イミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有しているため、該抽出物を摂取することにより、例えば抗酸化作用及び/又は抗疲労作用を発揮し得る。
According to the extract which is soluble in one physiologically acceptable liquid medium of the present invention or is extracted using a physiologically acceptable liquid medium as an extraction medium, imidazole dipeptides, in particular, very abundant quantities Therefore, by ingesting the extract, for example, it can exhibit an antioxidant effect and / or an anti-fatigue effect.
また、本発明の1つの生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物の製造方法によれば、イミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有する該抽出物を製造することができる。そのため、該抽出物を摂取することにより、例えば抗酸化作用及び/又は抗疲労作用を発揮し得る。
In addition, according to the method for producing an extract that is soluble in one physiologically acceptable liquid medium of the present invention or is extracted using a physiologically acceptable liquid medium as an extraction medium, imidazole dipeptide, The extract containing a very abundant amount of valenin can be produced. Therefore, by taking the extract, for example, an antioxidant action and / or an anti-fatigue action can be exhibited.
本発明の実施形態として、アカマンボウ由来の生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法を、添付する図面に基づいて詳細に述べる。
As an embodiment of the present invention, an extract which is soluble in a physiologically acceptable liquid medium derived from red sea cucumber or is extracted using a physiologically acceptable liquid medium as an extraction medium and a method for producing the same are attached. This will be described in detail with reference to the drawings.
<第1の実施形態>
図1は、本実施形態のアカマンボウ由来の生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本実施形態においては、「水溶性抽出物」。以下、本実施形態においては代表して「水溶性抽出物」と表記する。)の製造工程を示すフローである。本実施形態の水溶性抽出物及びその製造方法においては、図1に示す各処理工程が、水溶性抽出物の製造方法における全工程又はその一部となり得る。従って、本実施形態の水溶性抽出物の製造方法は、必ずしも図1に示す各処理工程の全てを含むことを要しない。また、図2は、本実施形態のアカマンボウ100の切断箇所及び部位を示すアカマンボウ100の一部を示す写真である。 <First Embodiment>
FIG. 1 shows an extract (in this embodiment, which is soluble in a physiologically acceptable liquid medium derived from red sea cucumber of this embodiment or extracted using a physiologically acceptable liquid medium as an extraction medium. This is a flow showing the manufacturing process of “water-soluble extract.” Hereinafter, in this embodiment, it is represented as “water-soluble extract” as a representative. In the water-soluble extract and the method for producing the same of the present embodiment, each processing step shown in FIG. 1 can be all or part of the steps in the method for producing a water-soluble extract. Therefore, the manufacturing method of the water-soluble extract of this embodiment does not necessarily include all the processing steps shown in FIG. FIG. 2 is a photograph showing a part of the red bowfish 100 showing the cut part and the site of the red bowfish 100 of the present embodiment.
図1は、本実施形態のアカマンボウ由来の生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本実施形態においては、「水溶性抽出物」。以下、本実施形態においては代表して「水溶性抽出物」と表記する。)の製造工程を示すフローである。本実施形態の水溶性抽出物及びその製造方法においては、図1に示す各処理工程が、水溶性抽出物の製造方法における全工程又はその一部となり得る。従って、本実施形態の水溶性抽出物の製造方法は、必ずしも図1に示す各処理工程の全てを含むことを要しない。また、図2は、本実施形態のアカマンボウ100の切断箇所及び部位を示すアカマンボウ100の一部を示す写真である。 <First Embodiment>
FIG. 1 shows an extract (in this embodiment, which is soluble in a physiologically acceptable liquid medium derived from red sea cucumber of this embodiment or extracted using a physiologically acceptable liquid medium as an extraction medium. This is a flow showing the manufacturing process of “water-soluble extract.” Hereinafter, in this embodiment, it is represented as “water-soluble extract” as a representative. In the water-soluble extract and the method for producing the same of the present embodiment, each processing step shown in FIG. 1 can be all or part of the steps in the method for producing a water-soluble extract. Therefore, the manufacturing method of the water-soluble extract of this embodiment does not necessarily include all the processing steps shown in FIG. FIG. 2 is a photograph showing a part of the red bowfish 100 showing the cut part and the site of the red bowfish 100 of the present embodiment.
具体的には、図1に示すように、漁獲されたアカマンボウ100が冷凍される(ステップS1)。その後、図2に示すように、アカマンボウ100の、頭部10、筋肉20(より細かく分類すれば、普通筋20a及び血合肉20b)、内臓部30、並びに尾ひれ90が、それぞれ分かれるように、略直線状にC1、C2、及びC3に沿って冷凍状態のアカマンボウ100を切断する、切断(解体)工程が行われる(ステップS2)。なお、図2においては、背びれを含む一部の部位が写真に表れていないが、表示されていない部位は、本実施形態の水溶性抽出物の原料ではないため、当該部位の説明を省略する。
Specifically, as shown in FIG. 1, the caught red sea bream 100 is frozen (step S1). After that, as shown in FIG. 2, the head 10, muscle 20 (normally muscle 20 a and blood 20 b), the internal organs 30, and the tail fin 90 of the red sea bream 100 are separated, respectively. A cutting (disassembling) step of cutting the frozen red sea bream 100 along C 1 , C 2 , and C 3 in a substantially straight line is performed (step S2). In addition, in FIG. 2, although the one part site | part including a back fin does not appear in a photograph, since the site | part which is not displayed is not the raw material of the water-soluble extract of this embodiment, description of the said site | part is abbreviate | omitted. .
ここで、図2におけるC1に示される切断は、本実施形態のアカマンボウ100のカマが筋肉20に含まれないように、かつ該カマにおける筋肉20側の端部の略接線方向に沿って実施される。また、図2におけるC2に示される切断は、本実施形態のアカマンボウ100の目と口が頭部10に含まれるように実施される。加えて、C3に示される切断は、本実施形態のアカマンボウ100の筋肉20が、極力、尾ひれ90に含まれないように実施される。なお、本実施形態においては、尾ひれ90は、本実施形態の水溶性抽出物の原料ではないため、当該部位の説明を省略する。なお、本実施形態の切断(解体)工程においては、公知のバンドソー装置が用いられているが、該工程においてアカマンボウを切断する手段は、該バンドソー装置に限定されない。C1、C2、及びC3に沿って冷凍状態のアカマンボウを切断することができる他の公知の切断方法も採用され得る。
Here, cutting as shown in C 1 in FIG. 2, as sickle of red sunfish 100 of the present embodiment is not included in the muscle 20, and along a substantially tangential direction of the end portion of the muscle 20 side of the hook To be implemented. Further, the cutting shown in C 2 in FIG. 2, the eyes and mouth of the red sunfish 100 of the present embodiment is performed as included in the head 10. In addition, the cutting shown in C 3, the muscles 20 of red sunfish 100 of this embodiment is carried out as much as possible, not included in the tail fin 90. In the present embodiment, the tail fin 90 is not a raw material for the water-soluble extract of the present embodiment, and thus the description of the part is omitted. In the cutting (disassembling) step of the present embodiment, a known band saw device is used, but means for cutting the red bowfish in the step is not limited to the band saw device. Other known cutting methods that can cut frozen red sea cucumbers along C 1 , C 2 , and C 3 may also be employed.
その後、公知のチョッパー装置(例えば、株式会社なんつね社製、型式:MC-22)による細片化を行うために、該チョッパー装置に導入することが可能となる程度に、冷凍状態であったアカマンボウ100の各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)を、それぞれ完全に又は不完全に解凍する。その後、該チョッパー装置を用いた細片化工程が行われることにより、例えば、10mmφの貫通孔を備えたプレートから細片化されたミンチ状の該各部位を得ることができる。なお、本実施形態の細片化工程においては、公知のチョッパー装置が用いられているが、該工程において細片化された該各部位を得る手段は、該チョッパー装置に限定されない。例えば、公知のサイレントカッターも、細片化工程において採用され得る。
Thereafter, it was in a frozen state to the extent that it could be introduced into the chopper device in order to perform fragmentation with a known chopper device (for example, model: MC-22, manufactured by NANTUNE Co., Ltd.). Each part (head 10, normal muscle 20a, blood joint meat 20b, internal organs 30, skin 40) of red sea bream 100 is thawed completely or incompletely. Thereafter, by performing a fragmentation step using the chopper device, for example, each of the minced portions that are fragmented from a plate having a through hole of 10 mmφ can be obtained. In the stripping step of the present embodiment, a known chopper device is used. However, means for obtaining the respective parts that are stripped in the step are not limited to the chopper device. For example, a known silent cutter can also be employed in the fragmentation process.
[アカマンボウ由来の細片化された各部位のイミダゾールジペプチド含有量の分析]
ここで、本発明者は、本実施形態の細片化された各部位が含有する、バレニンを含むイミダゾールジペプチドの量について分析を行った。具体的には、上述のように細片化された各部位から、過塩素酸抽出エキスを調製した上で、公知のアミノ酸自動分析計を用いて、図2に示す各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)の細片化された各部位に関する遊離アミノ酸及び結合アミノ酸に関する分析を行った。 [Analysis of content of imidazole dipeptide at each fragmented site of red squirrel]
Here, this inventor analyzed about the quantity of the imidazole dipeptide containing a barenine which each fragmented site | part of this embodiment contains. Specifically, after preparing a perchloric acid extract from each of the parts fragmented as described above, each of the parts shown in FIG. Analysis of free amino acids and bound amino acids for each segmented portion of thenormal muscle 20a, the blood meat 20b, the internal organs 30, and the skin 40) was performed.
ここで、本発明者は、本実施形態の細片化された各部位が含有する、バレニンを含むイミダゾールジペプチドの量について分析を行った。具体的には、上述のように細片化された各部位から、過塩素酸抽出エキスを調製した上で、公知のアミノ酸自動分析計を用いて、図2に示す各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)の細片化された各部位に関する遊離アミノ酸及び結合アミノ酸に関する分析を行った。 [Analysis of content of imidazole dipeptide at each fragmented site of red squirrel]
Here, this inventor analyzed about the quantity of the imidazole dipeptide containing a barenine which each fragmented site | part of this embodiment contains. Specifically, after preparing a perchloric acid extract from each of the parts fragmented as described above, each of the parts shown in FIG. Analysis of free amino acids and bound amino acids for each segmented portion of the
なお、表1における「Bal.」は「バレニンの含有量」を意味する。また、「Ans.」は「アンセリンの含有量」を意味し、「Cal.」は「カルノシンの含有量」を意味する。従って、表1における「合計(Imd.)」は、イミダゾールジペプチドの含有量を意味する。理解を容易にするために、各数値の下段には、イミダゾールジペプチドの含有量に対する比率(%)がカッコ書きによって表示されている。また、表1における各欄における「±」以降は、標準偏差を意味する。また、表1における分析対象としての皮部40は、筋肉20の部位の皮である。加えて、表1及び後述する表2における各数値における一の位の値は四捨五入している。
In Table 1, “Bal.” Means “valenin content”. “Ans.” Means “anserine content” and “Cal.” Means “carnosine content”. Therefore, “total (Imd.)” In Table 1 means the content of imidazole dipeptide. In order to facilitate understanding, the lower part of each numerical value displays the ratio (%) to the content of imidazole dipeptide in parentheses. In addition, after “±” in each column in Table 1, it means standard deviation. Further, the skin part 40 as the analysis target in Table 1 is a skin of the site of the muscle 20. In addition, the value of the first place in each numerical value in Table 1 and Table 2 described later is rounded off.
また、この分析においては、塩酸加水分解して結合アミノ酸を分析することにより、高濃度の3-メチルヒスチジンが検出された結果に基づいて、バレニンの存在が明らかとなった。また、バレニンの標準品を用いた加水分解液中の3-メチルヒスチジンに基づいてバレニンの量を定量することにより、細片化された各部位中のバレニンの量が定量された。
Also, in this analysis, the presence of valenin was clarified based on the result of detection of high concentrations of 3-methylhistidine by analyzing the bound amino acids by hydrolysis with hydrochloric acid. In addition, by quantifying the amount of valerin based on 3-methylhistidine in the hydrolyzate using a standard product of valenin, the amount of valerin in each segmented portion was quantified.
表1に示すように、この分析により、細片化された各部位中のバレニンを含むイミダゾールジペプチドの量に関する下記の(1)~(4)の特徴が明らかとなった。
(1)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(頭部、内臓、及び皮)も、可食部(普通筋)に匹敵する量のバレニンを含んでいること。
(2)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(内臓、及び皮)が含有するイミダゾールジペプチドの量は、該可食部(普通筋)が含有するイミダゾールジペプチドの量よりも顕著に多いこと。
(3)アカマンボウの、いわゆる可食部(普通筋)が含有するイミダゾールジペプチドの種類ごとの量と、該可食部(普通筋)と異なる部位(特に、内臓及び皮)が含有するイミダゾールジペプチドの種類ごとの量とが顕著に異なっていること。
(4)アカマンボウの普通筋と比較して、血合肉のイミダゾールジペプチド(バレニンを含む)の量のバラつき(標準偏差)が非常に大きいこと。 As shown in Table 1, this analysis revealed the following characteristics (1) to (4) regarding the amount of imidazole dipeptide containing valerin in each segmented portion.
(1) The part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
(2) The amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
(3) The amount of each kind of imidazole dipeptide contained in the so-called edible part (ordinary muscle) of red squirrel and the imidazole dipeptide contained in a part (particularly, viscera and skin) different from the edible part (ordinary muscle) The amount of each type is significantly different.
(4) The variation (standard deviation) in the amount of imidazole dipeptide (including valerine) in the blood meat is very large compared to the common muscle of red sea bream.
(1)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(頭部、内臓、及び皮)も、可食部(普通筋)に匹敵する量のバレニンを含んでいること。
(2)アカマンボウの、いわゆる可食部(普通筋)と異なる部位(内臓、及び皮)が含有するイミダゾールジペプチドの量は、該可食部(普通筋)が含有するイミダゾールジペプチドの量よりも顕著に多いこと。
(3)アカマンボウの、いわゆる可食部(普通筋)が含有するイミダゾールジペプチドの種類ごとの量と、該可食部(普通筋)と異なる部位(特に、内臓及び皮)が含有するイミダゾールジペプチドの種類ごとの量とが顕著に異なっていること。
(4)アカマンボウの普通筋と比較して、血合肉のイミダゾールジペプチド(バレニンを含む)の量のバラつき(標準偏差)が非常に大きいこと。 As shown in Table 1, this analysis revealed the following characteristics (1) to (4) regarding the amount of imidazole dipeptide containing valerin in each segmented portion.
(1) The part (head, internal organs, and skin) different from the so-called edible part (ordinary muscle) of the red sea bream also contains an amount of valenin comparable to that of the edible part (ordinary muscle).
(2) The amount of imidazole dipeptide contained in a portion (internal organs and skin) different from the so-called edible part (normal muscle) of the red squirrel is more than the amount of imidazole dipeptide contained in the edible part (normal muscle) Remarkably many.
(3) The amount of each kind of imidazole dipeptide contained in the so-called edible part (ordinary muscle) of red squirrel and the imidazole dipeptide contained in a part (particularly, viscera and skin) different from the edible part (ordinary muscle) The amount of each type is significantly different.
(4) The variation (standard deviation) in the amount of imidazole dipeptide (including valerine) in the blood meat is very large compared to the common muscle of red sea bream.
なお、上述の特徴の(1)に関してより具体的に説明すれば、少なくともアカマンボウ100由来の細片化された各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)が含有するバレニンの量は、ミンククジラの背肉赤肉が含有するバレニンの量と同等、又は該バレニンの量よりかなり多いと言える。また、興味深いことに、表1の普通筋20aの中でも、普通筋20a中心から頭側の普通筋20aのバレニンの含有量、及びイミダゾールジペプチドの含有量が、普通筋20a中心から尾側の普通筋20aのバレニンの含有量、及びイミダゾールジペプチドの含有量よりも、約10%多いことが確認された。
More specifically, the above feature (1) will be described in more detail. At least each segmented portion (head 10, normal muscle 20 a, blood meat 20 b, internal organ 30, skin part derived from red sea bream 100) It can be said that the amount of barenine contained in 40) is equivalent to or much larger than the amount of barenine contained in the minced whale red meat. Interestingly, among the normal muscles 20a in Table 1, the content of valenin from the center of the normal muscle 20a to the head side normal muscle 20a and the content of imidazole dipeptide are the same as the normal muscle 20a from the center of the normal muscle 20a. It was confirmed that the content of valenin of 20a and the content of imidazole dipeptide were about 10% higher.
なお、本実施形態においては、「普通筋20a中心」の位置は、頭部10の先端(口部の先端)から普通筋20aの尾側の端(従って、尾ひれ90を含まない)までの長さ(図2における「L」)を1としたときの、頭側先端から0.5の位置と定義される。従って、バレニンの含有量が多い普通筋20aをより確度高く得るためには、頭側先端から0.4以下までの普通筋20aを含む普通筋20aからイミダゾールジペプチド及び/又はバレニンを得ることは好適な一態様である。
In the present embodiment, the position of the “center of the normal muscle 20a” is the length from the tip of the head 10 (tip of the mouth) to the tail-side end of the normal muscle 20a (and thus not including the tail fin 90). This is defined as a position of 0.5 from the front end when “L” in FIG. 2 is 1. Therefore, in order to obtain the normal muscle 20a having a high content of valenin with higher accuracy, it is preferable to obtain imidazole dipeptide and / or valenin from the normal muscle 20a including the normal muscle 20a from the head side tip to 0.4 or less. This is one aspect.
本実施形態においては、その後、細片化された各部位を約60~約100℃の抽出媒体としての水(イオン交換水)に接触させる。より具体的には、細片化された各部位が、公知の容器内の約60℃~約100℃の該抽出媒体中に浸漬される抽出工程(ステップS3)が行われる。なお、本実施形態の抽出工程においては、意図的な該抽出媒体の撹拌は行われていないが、意図的に該抽出媒体を撹拌することも採用し得る一態様である。
In this embodiment, each segmented portion is then brought into contact with water (ion exchange water) as an extraction medium at about 60 to about 100 ° C. More specifically, an extraction step (step S3) is performed in which each segmented portion is immersed in the extraction medium at about 60 ° C. to about 100 ° C. in a known container. In addition, in the extraction process of this embodiment, although the stirring of this extraction medium is not performed intentionally, stirring this extraction medium intentionally is also one aspect | mode which can be employ | adopted.
その後、本実施形態においては、細片化された各部位が該抽出媒体中に浸漬されてから約2時間後に、該細片化された各部位からの水溶性抽出物を含有する該抽出媒体(本実施形態においては、水溶液)を、遠心分離機を用いて該各部位(残渣として取り扱われ得る)と分離する、分離工程が行われる(ステップS4)。具体的には、300メッシュのろ布を用いた遠心ろ過処理を行うことにより、本実施形態の水溶性抽出物を製造することができる。なお、本実施形態の水溶性抽出物は、液状である。また、本実施形態の分離工程においては、300メッシュのろ布を用いた遠心ろ過処理が採用されているが、本実施形態の分離工程はそのような態様に限定されない。公知の分離工程(例えば、遠心沈降による分離処理)も採用し得る他の一態様である。
Thereafter, in this embodiment, about 2 hours after each segmented portion is immersed in the extraction medium, the extraction medium containing a water-soluble extract from each segmented portion. In this embodiment, a separation process is performed in which the aqueous solution is separated from the respective parts (which can be handled as a residue) using a centrifuge (step S4). Specifically, the water-soluble extract of this embodiment can be produced by performing centrifugal filtration using a 300-mesh filter cloth. In addition, the water-soluble extract of this embodiment is liquid. In the separation process of the present embodiment, centrifugal filtration using a 300 mesh filter cloth is employed, but the separation process of the present embodiment is not limited to such a mode. This is another aspect in which a known separation step (for example, separation treatment by centrifugal sedimentation) can also be employed.
<第1の実施形態の変形例(1)>
本変形例においては、図1に示すように、第1の実施形態の水溶性抽出物の製造工程によって製造された水溶性抽出物をさらに濃縮することにより、より豊富な量のイミダゾールジペプチド又はバレニンを含有する濃縮抽出物としての水溶性抽出物(以下、単に「濃縮抽出物」ともいう。)を製造するための濃縮工程(ステップS5)が行われ得る。例えば、約1時間~約8時間、温度が約60℃であって、減圧(例えば、0.03MPa)状態の空間内に、第1の実施形態の水溶性抽出物を攪拌する又は静置させることにより、濃縮抽出物を製造することができる。なお、本変形例の濃縮工程においては、前述の処理条件が採用されているが、本変形例の濃縮工程はそのような態様に限定されない。後述する精製工程とは異なる公知の他の濃縮工程も採用し得る他の一態様である。また、本変形例の濃縮工程が行われる前に、殺菌処理(例えば、加熱処理)が行われることも、採用し得る他の一態様である。また、濃縮工程(ステップS5)において、第1の実施形態の水溶性抽出物を攪拌する又は静置させる温度が20℃以上、30℃以上、40℃以上、又は50℃以上であれば、本変形例の効果の少なくとも一部が奏され得る。 <Modification Example (1) of First Embodiment>
In this modified example, as shown in FIG. 1, by further concentrating the water-soluble extract produced by the water-soluble extract production process of the first embodiment, a more abundant amount of imidazole dipeptide or valenin A concentration step (step S5) for producing a water-soluble extract (hereinafter also simply referred to as “concentrated extract”) as a concentrated extract containing sucrose may be performed. For example, the water-soluble extract of the first embodiment is stirred or allowed to stand in a space of about 60 ° C. for about 1 hour to about 8 hours and at a reduced pressure (eg, 0.03 MPa). Thus, a concentrated extract can be produced. In addition, in the concentration process of this modification, the above-mentioned processing conditions are adopted, but the concentration process of this modification is not limited to such an embodiment. This is another embodiment in which another known concentration step different from the purification step described later can also be employed. Moreover, it is another one aspect | mode which can employ | adopt that a sterilization process (for example, heat processing) is performed before the concentration process of this modification is performed. In the concentration step (step S5), if the temperature at which the water-soluble extract of the first embodiment is stirred or allowed to stand is 20 ° C or higher, 30 ° C or higher, 40 ° C or higher, or 50 ° C or higher, At least some of the effects of the modification can be achieved.
本変形例においては、図1に示すように、第1の実施形態の水溶性抽出物の製造工程によって製造された水溶性抽出物をさらに濃縮することにより、より豊富な量のイミダゾールジペプチド又はバレニンを含有する濃縮抽出物としての水溶性抽出物(以下、単に「濃縮抽出物」ともいう。)を製造するための濃縮工程(ステップS5)が行われ得る。例えば、約1時間~約8時間、温度が約60℃であって、減圧(例えば、0.03MPa)状態の空間内に、第1の実施形態の水溶性抽出物を攪拌する又は静置させることにより、濃縮抽出物を製造することができる。なお、本変形例の濃縮工程においては、前述の処理条件が採用されているが、本変形例の濃縮工程はそのような態様に限定されない。後述する精製工程とは異なる公知の他の濃縮工程も採用し得る他の一態様である。また、本変形例の濃縮工程が行われる前に、殺菌処理(例えば、加熱処理)が行われることも、採用し得る他の一態様である。また、濃縮工程(ステップS5)において、第1の実施形態の水溶性抽出物を攪拌する又は静置させる温度が20℃以上、30℃以上、40℃以上、又は50℃以上であれば、本変形例の効果の少なくとも一部が奏され得る。 <Modification Example (1) of First Embodiment>
In this modified example, as shown in FIG. 1, by further concentrating the water-soluble extract produced by the water-soluble extract production process of the first embodiment, a more abundant amount of imidazole dipeptide or valenin A concentration step (step S5) for producing a water-soluble extract (hereinafter also simply referred to as “concentrated extract”) as a concentrated extract containing sucrose may be performed. For example, the water-soluble extract of the first embodiment is stirred or allowed to stand in a space of about 60 ° C. for about 1 hour to about 8 hours and at a reduced pressure (eg, 0.03 MPa). Thus, a concentrated extract can be produced. In addition, in the concentration process of this modification, the above-mentioned processing conditions are adopted, but the concentration process of this modification is not limited to such an embodiment. This is another embodiment in which another known concentration step different from the purification step described later can also be employed. Moreover, it is another one aspect | mode which can employ | adopt that a sterilization process (for example, heat processing) is performed before the concentration process of this modification is performed. In the concentration step (step S5), if the temperature at which the water-soluble extract of the first embodiment is stirred or allowed to stand is 20 ° C or higher, 30 ° C or higher, 40 ° C or higher, or 50 ° C or higher, At least some of the effects of the modification can be achieved.
ここで、本変形例の濃縮工程によって得られた濃縮抽出物が含有するバレニンの量を分析した結果、例えば、水分を約75wt%含有する(換言すれば、固形分が約25wt%である)濃縮抽出物を試料とした場合は、濃縮抽出物の総量に対するバレニンの含有量は、5wt%以上(より狭義には、9wt%以上)であることが確認された。従って、本変形例の濃縮工程によって得られた濃縮抽出物が含有するイミダゾールジペプチドの量も、5wt%以上(より狭義には、9wt%以上)含まれていることが明らかとなった。
Here, as a result of analyzing the amount of valenin contained in the concentrated extract obtained by the concentration step of this modification, for example, it contains about 75 wt% of water (in other words, the solid content is about 25 wt%). When the concentrated extract was used as a sample, it was confirmed that the content of valerin relative to the total amount of the concentrated extract was 5 wt% or more (more narrowly, 9 wt% or more). Therefore, it has been clarified that the amount of imidazole dipeptide contained in the concentrated extract obtained by the concentration step of this modification is also contained in an amount of 5 wt% or more (more narrowly, 9 wt% or more).
<第1の実施形態の変形例(2)>
本変形例においては、図1に示すように、第1の実施形態の変形例(1)の濃縮抽出物としての生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本変形例においては、「水溶性抽出物」。以下、本変形例においては代表して「水溶性抽出物」と表記する。)の製造工程によって製造された濃縮抽出物を乾燥させることにより、乾燥抽出物を得る乾燥工程(ステップS6)が行われ得る。 <Modification (1) of the first embodiment>
In this modification, as shown in FIG. 1, a soluble or physiologically acceptable liquid that is soluble in a physiologically acceptable liquid medium as the concentrated extract of the modification (1) of the first embodiment. Manufactured by a manufacturing process of an extract that is extracted using a medium as an extraction medium (in this variation, “water-soluble extract”. Hereinafter, in this variation, it is represented as “water-soluble extract” as a representative). The drying process (step S6) which obtains a dry extract by drying the concentrated extract made can be performed.
本変形例においては、図1に示すように、第1の実施形態の変形例(1)の濃縮抽出物としての生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本変形例においては、「水溶性抽出物」。以下、本変形例においては代表して「水溶性抽出物」と表記する。)の製造工程によって製造された濃縮抽出物を乾燥させることにより、乾燥抽出物を得る乾燥工程(ステップS6)が行われ得る。 <Modification (1) of the first embodiment>
In this modification, as shown in FIG. 1, a soluble or physiologically acceptable liquid that is soluble in a physiologically acceptable liquid medium as the concentrated extract of the modification (1) of the first embodiment. Manufactured by a manufacturing process of an extract that is extracted using a medium as an extraction medium (in this variation, “water-soluble extract”. Hereinafter, in this variation, it is represented as “water-soluble extract” as a representative). The drying process (step S6) which obtains a dry extract by drying the concentrated extract made can be performed.
本変形例においては、乾燥工程の代表的な例としての、真空乾燥(減圧乾燥を含む)工程又は凍結乾燥工程が行われる。ここで、本変形例における「真空乾燥(又は減圧乾燥)工程」とは、加熱しつつ真空状態(又は減圧状態)で乾燥させる工程を意味する。また、本変形例における「凍結乾燥工程」は、「凍結真空乾燥工程」又は「凍結減圧乾燥工程」を含む。
In this modification, a vacuum drying (including reduced pressure drying) process or a freeze drying process is performed as a typical example of the drying process. Here, the “vacuum drying (or reduced pressure drying) step” in this modification means a step of drying in a vacuum state (or reduced pressure state) while heating. Further, the “freeze-drying step” in the present modification includes a “freeze-vacuum drying step” or a “freeze-decompression drying step”.
なお、本変形例の乾燥抽出物が含有するイミダゾールジペプチド(特に、バレニン)の量が顕著に(例えば、約20%以上)損なわれない限り、前述の2種類の乾燥工程の代わりに、熱風乾燥、マイクロ波乾燥、過熱水蒸気乾燥、フライ乾燥、減圧フライ乾燥、ドラム乾燥、又は天日乾燥による乾燥工程を採用することもできる。
As long as the amount of imidazole dipeptide (particularly, valerin) contained in the dry extract of this modification is not significantly impaired (for example, about 20% or more), hot air drying is used instead of the above two types of drying steps. It is also possible to employ a drying process by microwave drying, superheated steam drying, fly drying, reduced-pressure fly drying, drum drying, or sun drying.
例えば、真空乾燥工程が採用される場合、公知の方法及び装置を用いることができる。例えば、連続式ベルト乾燥装置又は真空ドラム式乾燥装置が採用され得る。本実施形態においては、大気圧を0としたゲージ圧-0.093MPaの圧力下であって約60℃の環境下において、約12時間~約72時間、第1の実施形態の変形例(1)の濃縮抽出物を攪拌する又は静置させることによって、本変形例の乾燥抽出物を形成することができる。なお、この真空乾燥工程において、第1の実施形態の変形例(1)の濃縮抽出物を攪拌する又は静置させる温度が20℃以上、30℃以上、40℃以上、又は50℃以上であれば、本変形例の効果の少なくとも一部が奏され得る。
For example, when a vacuum drying process is employed, a known method and apparatus can be used. For example, a continuous belt dryer or a vacuum drum dryer may be employed. In the present embodiment, a modification (1) of the first embodiment is performed for about 12 hours to about 72 hours in an environment of about 60 ° C. under a gauge pressure of −0.093 MPa with the atmospheric pressure being 0. The dried extract of this modification can be formed by stirring or leaving the concentrated extract of). In this vacuum drying step, the temperature at which the concentrated extract of the modified example (1) of the first embodiment is stirred or allowed to stand is 20 ° C or higher, 30 ° C or higher, 40 ° C or higher, or 50 ° C or higher. For example, at least a part of the effects of the present modification can be achieved.
次に、凍結乾燥工程が採用される場合も、公知の方法及び装置を用いることができる。例えば、凍結乾燥装置(協和真空技術社製、型式:RL4522BS)が採用され得る。本実施形態においては、約266Paの圧力下であって約-20℃の環境下において、約168時間、第1の実施形態の変形例(1)の濃縮抽出物を攪拌する又は静置させることによって、バレニンを7wt%(より狭義には10wt%以上、又は15wt%以上、あるいは20wt%以上、さらに狭義には25wt%以上、非常に狭義には30wt%以上)含有する本変形例の乾燥抽出物を形成することができる。
Next, when a freeze-drying process is employed, a known method and apparatus can be used. For example, a freeze-drying apparatus (Kyowa Vacuum Technology Co., Ltd., model: RL4522BS) can be employed. In the present embodiment, the concentrated extract of the modified example (1) of the first embodiment is stirred or allowed to stand for about 168 hours under a pressure of about 266 Pa and in an environment of about −20 ° C. The dry extraction of this modification containing 7 wt% (more narrowly, 10 wt% or more, 15 wt% or more, or 20 wt% or more, more narrowly defined 25 wt% or more, very narrowly defined 30 wt% or more) Things can be formed.
なお、真空乾燥又は凍結乾燥に代表される本変形例の乾燥抽出物の水分量は、適宜、公知の手段によって調整され得る。但し、運搬の容易化及び/又は取り扱いの容易化の観点から、該水分量が本変形例の乾燥抽出物の0wt%超10wt%以下であることは好適な一態様である。なお、前述の観点から言えば、該水分量が本変形例の乾燥抽出物の5wt%以下であることがより好ましく、本変形例の乾燥抽出物の3wt%以下であることが更に好ましい。
It should be noted that the moisture content of the dried extract of the present modification represented by vacuum drying or freeze drying can be adjusted as appropriate by known means. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the moisture content is more than 0 wt% and not more than 10 wt% of the dry extract of this modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the dry extract of the present modification, and further preferably 3 wt% or less of the dry extract of the present modification.
その後、本変形例の乾燥抽出物をさらに粉砕することによって粗粉体を得るための粉末化工程(ステップS7)が行われることは採用し得る一態様である。本実施形態においては、例えば、公知のハンマーミル(例えば、ホソカワミクロン株式会社製ハンマーミル)が採用され得る。より具体的には、粒度が2mm以下になるように設定された処理条件によって、本変形例の乾燥抽出物が粉末化され得る。
Thereafter, it is an aspect that can be adopted that a powdering step (step S7) for obtaining a coarse powder by further crushing the dried extract of the present modification is performed. In the present embodiment, for example, a known hammer mill (for example, a hammer mill manufactured by Hosokawa Micron Corporation) may be employed. More specifically, the dry extract of this modification can be pulverized under the processing conditions set so that the particle size is 2 mm or less.
なお、本変形例の乾燥抽出物が含有するイミダゾールジペプチド(特に、バレニン)の量が顕著に(例えば、約20%以上)損なわれない限り、前述のハンマーミルの代わりに、ピンミル、ボールミル、インパクトミル、エッジランナーミル、ローラーミル、振動ミル、円錐形粉砕機、ジェットミル、又はその他の公知の機械式衝撃/粉砕装置を採用することもできる。
In addition, as long as the amount of imidazole dipeptide (particularly, valerin) contained in the dry extract of this modification is not significantly impaired (for example, about 20% or more), instead of the above-mentioned hammer mill, a pin mill, a ball mill, an impact Mills, edge runner mills, roller mills, vibration mills, conical crushers, jet mills, or other known mechanical impact / grinding devices can also be employed.
上述の各工程を経て、アカマンボウ100由来である、本実施形態の粗粉体としての乾燥抽出物(以下、単に「粗粉体」ともいう)を製造することができる。
Through the above-described steps, a dry extract (hereinafter, also simply referred to as “coarse powder”) as the coarse powder of the present embodiment, which is derived from the red pepper 100, can be produced.
ここで、本発明者は、本変形例の粉末化工程によって得られた粗粉体としての乾燥抽出物が含有するバレニンの量を分析した。その結果、例えば、アカマンボウ100の筋肉20に着目すれば、水分を約5wt%含有する(換言すれば、固形分が約95wt%である)粗粉体を試料とした場合は、粗粉体の総量に対するバレニンの含有量は、7wt%(より狭義には10wt%以上、又は15wt%以上、あるいは20wt%以上、さらに狭義には25wt%以上、非常に狭義には30wt%以上)という非常に高い含有量であることが確認された。従って、本変形例の粉末化工程によって得られた粗粉体が含有するイミダゾールジペプチドの量も、7wt%(より狭義には10wt%以上、又は15wt%以上、あるいは20wt%以上、さらに狭義には25wt%以上、非常に狭義には30wt%以上)含まれていることが明らかとなった。
Here, the present inventor analyzed the amount of valenin contained in the dry extract as a coarse powder obtained by the powdering step of the present modification. As a result, for example, when paying attention to the muscle 20 of the red squirrel bow 100, when a coarse powder containing about 5 wt% water (in other words, having a solid content of about 95 wt%) is used as a sample, the coarse powder The content of valerine with respect to the total amount of the material is 7 wt% (10 wt% or more in the narrow sense, or 15 wt% or more, or 20 wt% or more, 25 wt% or more in the narrow sense, 30 wt% or more in the very narrow sense). It was confirmed that the content was high. Therefore, the amount of imidazole dipeptide contained in the coarse powder obtained by the powdering step of this modification is also 7 wt% (more narrowly 10 wt% or more, 15 wt% or more, or 20 wt% or more, and more narrowly, 25 wt% or more, and in a very narrow sense, 30 wt% or more) was revealed.
なお、本変形例の粗粉体としての乾燥抽出物の水分量も、上述と同様に、適宜、公知の手段によって調整され得る。但し、運搬の容易化及び/又は取り扱いの容易化の観点から、該水分量が本変形例の粗粉体の0wt%超10wt%以下であることは好適な一態様である。なお、前述の観点から言えば、該水分量が本変形例の粗粉体の5wt%以下であることがより好ましく、本変形例の粗粉体の3wt%以下であることが更に好ましい。
It should be noted that the moisture content of the dried extract as the coarse powder of the present modification can be adjusted as appropriate by known means, as described above. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the water content is more than 0 wt% and not more than 10 wt% of the coarse powder of this modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the coarse powder of the present modification, and further preferably 3 wt% or less of the coarse powder of the present modification.
加えて、本変形例の粗粉体は、精製工程を経ずに製造された粗粉体である。より具体的には、該粗粉体は、例えば、非特許文献2において開示されている方法のように、該粗粉体を水等に溶解させた後、イオン交換樹脂(例えば、陽イオン交換樹脂)を利用してバレニンを含むイミダゾールジペプチドを抽出し精製する工程が行われずに得られた粗粉体である。従って、精製されていない粗粉体であっても、例えば抗酸化作用及び/又は抗疲労作用を発揮し得るイミダゾールジペプチド、特に、上述のように非常に豊富な量のバレニンを含有していることは、イミダゾールジペプチド及び/又はバレニンの歩留まり(収率を含む)の向上、製造工程の簡素化(製造時間の短縮化を含む)、製造コストの低減等、多くの利点を生み出すため、特筆に値する。
In addition, the coarse powder of this modified example is a coarse powder produced without undergoing a purification process. More specifically, the coarse powder is prepared by dissolving the coarse powder in water or the like, as in the method disclosed in Non-Patent Document 2, for example, and then using an ion exchange resin (for example, cation exchange). A crude powder obtained without performing a step of extracting and purifying imidazole dipeptide containing valenin using a resin. Therefore, even if the crude powder is not purified, it contains, for example, an imidazole dipeptide capable of exerting an antioxidant action and / or an anti-fatigue action, in particular, a very abundant amount of valenin as described above. Is worthy of note because it produces many advantages such as improving yield (including yield) of imidazole dipeptide and / or valenin, simplifying manufacturing process (including shortening manufacturing time), and reducing manufacturing cost. .
<第1の実施形態の変形例(3)>
本変形例においては、図1に示すように、第1の実施形態の変形例(2)の製造工程によって製造された粗粉体としての乾燥抽出物をさらに分級することにより、1mm未満(より好ましくは、0.8mm未満)の粒子径を有する粉体からなる微粉体としての乾燥抽出物(以下、単に「微粉体」ともいう)を得るための分級工程(ステップS8)が行われ得る。 <Modification (3) of the first embodiment>
In this modified example, as shown in FIG. 1, the dried extract as a coarse powder produced by the production process of the modified example (2) of the first embodiment is further classified to be less than 1 mm (more Preferably, a classification step (step S8) for obtaining a dry extract (hereinafter also simply referred to as “fine powder”) as a fine powder composed of a powder having a particle diameter of less than 0.8 mm) may be performed.
本変形例においては、図1に示すように、第1の実施形態の変形例(2)の製造工程によって製造された粗粉体としての乾燥抽出物をさらに分級することにより、1mm未満(より好ましくは、0.8mm未満)の粒子径を有する粉体からなる微粉体としての乾燥抽出物(以下、単に「微粉体」ともいう)を得るための分級工程(ステップS8)が行われ得る。 <Modification (3) of the first embodiment>
In this modified example, as shown in FIG. 1, the dried extract as a coarse powder produced by the production process of the modified example (2) of the first embodiment is further classified to be less than 1 mm (more Preferably, a classification step (step S8) for obtaining a dry extract (hereinafter also simply referred to as “fine powder”) as a fine powder composed of a powder having a particle diameter of less than 0.8 mm) may be performed.
本変形例の分級工程(ステップS8)を採用することにより、例えば、目開きが0.7mmの篩(ふるい)を通過する、微粉体のみを回収することができる。その結果、アカマンボウ100由来の本変形例の乾燥抽出物(1mm未満の粒子径を有する粉体からなる微粉体としての乾燥抽出物)を製造することができる。なお、第1の実施形態の変形例(2)における粉末化工程において採用されたハンマーミル等が分級機能をも備えている場合は、粉末化工程と分級工程とが同時に実施され得る。
By adopting the classification step (step S8) of this modification, for example, only fine powder that passes through a sieve having a sieve opening of 0.7 mm can be collected. As a result, it is possible to produce the dry extract of the present modification derived from the red squirrel 100 (the dry extract as a fine powder composed of a powder having a particle diameter of less than 1 mm). In addition, when the hammer mill etc. which were employ | adopted in the powdering process in the modification (2) of 1st Embodiment are also provided with the classification function, a powdering process and a classification process can be implemented simultaneously.
ここで、本発明者は、本変形例の分級工程によって得られた微粉体が含有するバレニンの量を分析した。その結果、例えば、アカマンボウ100の筋肉20に着目すれば、水分を約5wt%含有する(換言すれば、固形分が約95wt%である)微粉体を試料とした場合は、微粉体の総量に対するバレニンの含有量は、7wt%(より狭義には10wt%以上、又は15wt%以上、あるいは20wt%以上、さらに狭義には25wt%以上、非常に狭義には30wt%以上)という非常に高い含有量であることが確認された。従って、本変形例の分級工程によって得られた微粉体が含有するイミダゾールジペプチドの量も、7wt%(より狭義には10wt%以上、又は15wt%以上、あるいは20wt%以上、さらに狭義には25wt%以上、非常に狭義には30wt%以上)含まれていることが明らかとなった。なお、現段階において本発明者が確認できている最も高い結果を述べると、微粉体としての該乾燥抽出物の総量に対するバレニンのみの含有量として、約35wt%の値が得られていることは特筆に値する。
Here, the present inventor analyzed the amount of barenin contained in the fine powder obtained by the classification process of this modification. As a result, for example, when paying attention to the muscle 20 of the red squirrel bow 100, when a fine powder containing about 5 wt% water (in other words, having a solid content of about 95 wt%) is used as a sample, the total amount of fine powder The content of valerin is 7 wt% (10 wt% or more in a narrow sense, 15 wt% or more, or 20 wt% or more, 25 wt% or more in a narrow sense, 30 wt% or more in a very narrow sense) The amount was confirmed. Therefore, the amount of imidazole dipeptide contained in the fine powder obtained by the classification step of this modification is also 7 wt% (more narrowly 10 wt% or more, 15 wt% or more, or 20 wt% or more, and more narrowly 25 wt%). As described above, it was revealed that 30 wt% or more is contained in a very narrow sense. In addition, to describe the highest result that the present inventors have confirmed at this stage, the value of about 35 wt% is obtained as the content of only barenin relative to the total amount of the dry extract as a fine powder. Deserves special mention.
なお、別の視点で本変形例の微粉体を評価すると、例えば、アカマンボウ100の筋肉20に着目すれば、漁獲されたアカマンボウ100の筋肉20の質量(例えば、1kg)を基準としたときの、該筋肉20由来の乾燥抽出物(微粉体としての乾燥抽出物)の質量の比率(すなわち、収率)は、50g超(より狭義には、60g以上)であった。また、大変興味深いことに、微粉体としての該乾燥抽出物のうちのバレニンの含有量が占める割合の一例は、25wt%以上(より狭義には、30wt%以上)という極めて高い値であった。
When the fine powder of this modification is evaluated from another viewpoint, for example, when focusing on the muscle 20 of the red sea bream 100, when the mass (for example, 1 kg) of the captured muscle 20 of the red sea bream 100 is used as a reference The mass ratio (ie, yield) of the dry extract derived from the muscle 20 (dry extract as a fine powder) was more than 50 g (60 g or more in a narrow sense). Also, very interestingly, an example of the proportion of the content of valerin in the dry extract as a fine powder was an extremely high value of 25 wt% or more (more narrowly, 30 wt% or more).
なお、本変形例の微粉体としての乾燥抽出物の水分量も、上述と同様に、適宜、公知の手段によって調整され得る。但し、運搬の容易化及び/又は取り扱いの容易化の観点から、該水分量が本変形例の微粉体の0wt%超10wt%以下であることは好適な一態様である。なお、前述の観点から言えば、該水分量が本変形例の微粉体の5wt%以下であることがより好ましく、本変形例の微粉体の3wt%以下であることが更に好ましい。
It should be noted that the moisture content of the dry extract as the fine powder of the present modification can be adjusted as appropriate by known means, as described above. However, from the viewpoint of facilitating transportation and / or handling, it is a preferred embodiment that the water content is more than 0 wt% and not more than 10 wt% of the fine powder of the present modification. From the viewpoint described above, the water content is more preferably 5 wt% or less of the fine powder of the present modification, and further preferably 3 wt% or less of the fine powder of the present modification.
上述のとおり、本変形例における微粉体としての乾燥抽出物は、精製工程を経ずに製造された微粉体である。より具体的には、該微粉体は、例えば、非特許文献2において開示されている方法のように、該微粉体を水等に溶解させた後、イオン交換樹脂(例えば、陽イオン交換樹脂)を利用してバレニンを含むイミダゾールジペプチドを抽出し精製する工程が行われずに得られた微粉体である。従って、精製されていない微粉体としての微粉体であっても、例えば抗酸化作用及び/又は抗疲労作用を発揮し得るイミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有していることは、特筆に値する。
As described above, the dry extract as a fine powder in the present modification is a fine powder produced without undergoing a purification process. More specifically, the fine powder is obtained by dissolving the fine powder in water or the like, as in the method disclosed in Non-Patent Document 2, for example, and then an ion exchange resin (for example, a cation exchange resin). Is a fine powder obtained without performing the step of extracting and purifying imidazole dipeptide containing valenin. Therefore, even a fine powder as an unpurified fine powder contains, for example, an imidazole dipeptide capable of exerting an antioxidant action and / or an anti-fatigue action, in particular, a very abundant amount of valenin. Deserves special mention.
表2は、冷凍工程から分級工程までの各工程(ステップS1~S8)が行われたときの、普通筋20aの生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本変形例においては、「水溶性抽出物」。以下、本変形例においては代表して「水溶性抽出物」と表記する。)の表1に対応する分析結果の一例を示している。
Table 2 shows a soluble or physiologically acceptable liquid in a physiologically acceptable liquid medium of the normal muscle 20a when each process (steps S1 to S8) from the freezing process to the classification process is performed. Corresponds to Table 1 of extracts extracted using the medium as an extraction medium (in this variation, “water-soluble extract”. Hereinafter, in this variation, it is represented as “water-soluble extract” as a representative). An example of the analysis result is shown.
なお、この分析においては、塩酸加水分解して結合アミノ酸を分析することにより、高濃度の3-メチルヒスチジンが検出された結果に基づいて、バレニンの存在が明らかとなった。また、バレニンの標準品を用いた加水分解エキス中の3-メチルヒスチジンに基づいてバレニンの量を定量することにより、各部位の水溶性抽出物中のバレニンの量が定量された。
In this analysis, the presence of valenin was clarified based on the result of detection of a high concentration of 3-methylhistidine by analyzing the bound amino acid by hydrolysis with hydrochloric acid. Further, the amount of barenin in the water-soluble extract at each site was quantified by quantifying the amount of barenin based on 3-methylhistidine in the hydrolyzed extract using a standard product of barenine.
表2に示すように、第1の実施形態のステップS2によって切断された普通筋20aから製造された水溶性抽出物における、(バレニンを含む)イミダゾールジペプチドの含有量(例えば、表2における27850mg/100g)に対するバレニン含有量(例えば、表2における23870mg/100g)の比率が、約86%であった。この値は、表1における同基準の比率(約88%)とほぼ同等であるといえる。なお、説明の便宜上、前述の比率を、「イミダゾールジペプチド-バレニン比率」ともいう。
As shown in Table 2, the content of imidazole dipeptide (including valenin) in the water-soluble extract produced from the normal muscle 20a cut by step S2 of the first embodiment (for example, 27850 mg / day in Table 2) The ratio of the valenine content (for example, 23870 mg / 100 g in Table 2) to 100 g) was about 86%. This value can be said to be almost equivalent to the ratio (about 88%) of the same standard in Table 1. For convenience of explanation, the above ratio is also referred to as “imidazole dipeptide-valenine ratio”.
従って、本実施形態において製造された水溶性抽出物は、極めて高いバレニン含有量と、極めて高い「イミダゾールジペプチド-バレニン比率」を実現し得ることが確認された。加えて、本実施形態において製造された水溶性抽出物は、第1の実施形態のアカマンボウ由来の各部位のイミダゾールジペプチド含有量、バレニン含有量、及び前述の「イミダゾールジペプチド-バレニン比率」を、ほぼそのまま反映し得る物質であることが確認された。
Therefore, it was confirmed that the water-soluble extract produced in this embodiment can achieve an extremely high valenine content and an extremely high “imidazole dipeptide-valenine ratio”. In addition, the water-soluble extract produced in the present embodiment has the imidazole dipeptide content, the valenin content, and the aforementioned “imidazole dipeptide-valenine ratio” at each site derived from the red sea cucumber of the first embodiment, It was confirmed that the substance can be reflected almost as it is.
なお、第1の実施形態と同様に、本実施形態において製造された水溶性抽出物が含有するバレニンの量は、ミンククジラの背肉赤肉が含有するバレニンの量と同等、又は該バレニンの量よりかなり多いと言える。
As in the first embodiment, the amount of barenin contained in the water-soluble extract produced in the present embodiment is equal to the amount of ballenin contained in the minced whale back meat red meat, or It can be said that it is much more than the amount.
上述の結果及び他の実験結果を受け、本発明者らの分析と検討の結果、本実施形態において製造された水溶性抽出物が含有するバレニンの含有量、及びイミダゾールジペプチドの含有量、及び「イミダゾールジペプチド-バレニン比率」について、本発明者らは、下記の数値範囲を実現し得ることを知得した。
(1)水溶性抽出物全体の質量に対して、バレニンの含有量が7wt%以上(より狭義には、10wt%以上)である。
(2)水溶性抽出物全体の質量に対して、イミダゾールジペプチドの含有量が25wt%以上である。
(3)本実施形態の水溶性抽出物の「イミダゾールジペプチド-バレニン比率」については、イミダゾールジペプチド(但し、バレニンを含む)の含有量を1としたときの、該バレニンの含有量が、0.5以上0.97以下(より狭義には、0.75以上0.97以下)である。 Based on the above results and other experimental results, as a result of the analysis and examination by the present inventors, the content of valenin contained in the water-soluble extract produced in the present embodiment, the content of imidazole dipeptide, and “ Regarding the “imidazole dipeptide-valenine ratio”, the present inventors have found that the following numerical range can be realized.
(1) The content of valenin is 7 wt% or more (more narrowly, 10 wt% or more) based on the total mass of the water-soluble extract.
(2) The content of imidazole dipeptide is 25 wt% or more with respect to the mass of the entire water-soluble extract.
(3) Regarding the “imidazole dipeptide-valenine ratio” of the water-soluble extract of the present embodiment, when the content of imidazole dipeptide (including valenin) is 1, the content of valenin is 0. 5 or more and 0.97 or less (more narrowly, 0.75 or more and 0.97 or less).
(1)水溶性抽出物全体の質量に対して、バレニンの含有量が7wt%以上(より狭義には、10wt%以上)である。
(2)水溶性抽出物全体の質量に対して、イミダゾールジペプチドの含有量が25wt%以上である。
(3)本実施形態の水溶性抽出物の「イミダゾールジペプチド-バレニン比率」については、イミダゾールジペプチド(但し、バレニンを含む)の含有量を1としたときの、該バレニンの含有量が、0.5以上0.97以下(より狭義には、0.75以上0.97以下)である。 Based on the above results and other experimental results, as a result of the analysis and examination by the present inventors, the content of valenin contained in the water-soluble extract produced in the present embodiment, the content of imidazole dipeptide, and “ Regarding the “imidazole dipeptide-valenine ratio”, the present inventors have found that the following numerical range can be realized.
(1) The content of valenin is 7 wt% or more (more narrowly, 10 wt% or more) based on the total mass of the water-soluble extract.
(2) The content of imidazole dipeptide is 25 wt% or more with respect to the mass of the entire water-soluble extract.
(3) Regarding the “imidazole dipeptide-valenine ratio” of the water-soluble extract of the present embodiment, when the content of imidazole dipeptide (including valenin) is 1, the content of valenin is 0. 5 or more and 0.97 or less (more narrowly, 0.75 or more and 0.97 or less).
<第2の実施形態>
本実施形態の生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法においては、図3に示す各処理工程が、生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本実施形態においては、「水溶性抽出物」。以下、本実施形態においては、代表して「水溶性抽出物」と表記する。)の製造方法における全工程又はその一部となり得る。従って、本実施形態の水溶性抽出物の製造方法は、必ずしも図3に示す各処理工程の全てを含むことを要しない。また、第1の実施形態及びその各変形例(1)~(3)と重複する説明は省略され得る。 <Second Embodiment>
In the extract that is soluble in the physiologically acceptable liquid medium of the present embodiment or is extracted using the physiologically acceptable liquid medium as an extraction medium and the method for producing the same, each processing step shown in FIG. An extract that is soluble in a physiologically acceptable liquid medium or is extracted using a physiologically acceptable liquid medium as an extraction medium (in the present embodiment, a “water-soluble extract”. Hereinafter, in the present embodiment, Can be represented as “water-soluble extract” as a representative example) or a part thereof. Therefore, the manufacturing method of the water-soluble extract of this embodiment does not necessarily include all the processing steps shown in FIG. Further, the description overlapping with the first embodiment and the modifications (1) to (3) thereof may be omitted.
本実施形態の生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法においては、図3に示す各処理工程が、生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(本実施形態においては、「水溶性抽出物」。以下、本実施形態においては、代表して「水溶性抽出物」と表記する。)の製造方法における全工程又はその一部となり得る。従って、本実施形態の水溶性抽出物の製造方法は、必ずしも図3に示す各処理工程の全てを含むことを要しない。また、第1の実施形態及びその各変形例(1)~(3)と重複する説明は省略され得る。 <Second Embodiment>
In the extract that is soluble in the physiologically acceptable liquid medium of the present embodiment or is extracted using the physiologically acceptable liquid medium as an extraction medium and the method for producing the same, each processing step shown in FIG. An extract that is soluble in a physiologically acceptable liquid medium or is extracted using a physiologically acceptable liquid medium as an extraction medium (in the present embodiment, a “water-soluble extract”. Hereinafter, in the present embodiment, Can be represented as “water-soluble extract” as a representative example) or a part thereof. Therefore, the manufacturing method of the water-soluble extract of this embodiment does not necessarily include all the processing steps shown in FIG. Further, the description overlapping with the first embodiment and the modifications (1) to (3) thereof may be omitted.
具体的には、図3に示すように、第1の実施形態及びその各変形例(1)~(2)に示す、冷凍工程から乾燥工程(ステップS1~S6)まで、冷凍工程から粉末化工程までの各工程(ステップS1~S7)、又は冷凍工程から図示しない分級工程までの各工程(ステップS1~S8)が行われた後、あるいは、冷凍工程から分離工程(ステップS1~S4)が行われた後、本実施形態の精製工程(ステップS9)が行われる。
Specifically, as shown in FIG. 3, from the freezing step to the drying step (steps S1 to S6) shown in the first embodiment and the modifications (1) to (2) thereof, the freezing step to the pulverization are performed. After each process up to the process (steps S1 to S7), each process from the freezing process to the classification process (not shown) (steps S1 to S8), or after the freezing process is separated (steps S1 to S4) After being performed, the purification process (step S9) of this embodiment is performed.
本実施形態の精製工程(ステップS9)においては、非特許文献2において開示されている方法のように、乾燥抽出物又は粗粉体としての乾燥抽出物を水等に溶解させた後、イオン交換樹脂(例えば、陽イオン交換樹脂)を利用して、バレニンを含むイミダゾールジペプチドを抽出し精製する工程が行われる。その結果、第1の実施形態及びその各変形例(1)~(3)よりも豊富な含有率のイミダゾールジペプチド、及び豊富な含有率のバレニンを含有する水溶性抽出物を製造することができる。
In the purification step (step S9) of the present embodiment, after the dry extract or the dry extract as a coarse powder is dissolved in water or the like as in the method disclosed in Non-Patent Document 2, ion exchange is performed. Using a resin (for example, a cation exchange resin), a step of extracting and purifying imidazole dipeptide containing valenin is performed. As a result, it is possible to produce a water-soluble extract containing an imidazole dipeptide having a richer content than in the first embodiment and its modifications (1) to (3) and a rich content of valenin. .
なお、本実施形態の精製工程(ステップS9)が行われることによって得られる水溶性抽出物全体の質量に対するイミダゾールジペプチドの含有量及びバレニンの含有量の上限は特に限定されないため、それぞれの含有量の上限は、いわば100wt%未満といえる。敢えて上限値を言及すれば、より狭義には、該イミダゾールジペプチドの含有量及び該バレニンの含有量は99wt%以下であり、更に狭義には、95wt%以下である。また、この上限値の数値範囲については他の実施形態にも適用され得る。
In addition, since the upper limit of the content of imidazole dipeptide and the content of valenin with respect to the total mass of the water-soluble extract obtained by performing the purification step (step S9) of this embodiment is not particularly limited, It can be said that the upper limit is less than 100 wt%. If the upper limit is dared to be mentioned, the content of the imidazole dipeptide and the content of the valenine are 99 wt% or less in a narrower sense, and 95 wt% or less in a narrower sense. The numerical range of the upper limit value can be applied to other embodiments.
<その他の実施形態>
ところで、第1の実施形態及びその各変形例、並びに第2の実施形態においては、アカマンボウ100の各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)の特徴を知るために、個別に抽出工程(ステップS3)及び分離工程(ステップS4)、並びに必要に応じた濃縮工程(ステップS5)、乾燥工程(ステップS6)、粉末化工程(ステップS7)、分級工程(ステップS8)、又は精製工程(ステップS9)が行われているが、本実施形態はそのような態様に限定されない。 <Other embodiments>
By the way, in 1st Embodiment and its each modification, and 2nd Embodiment, each site | part (thehead 10, the normal muscle 20a, the blood muscle 20b, the internal organs 30, and the skin part 40) of the red sea bream 100. In order to know the characteristics, the extraction process (step S3) and the separation process (step S4), the concentration process (step S5), the drying process (step S6), the powdering process (step S7), and the classification as needed Although the process (step S8) or the purification process (step S9) is performed, the present embodiment is not limited to such an aspect.
ところで、第1の実施形態及びその各変形例、並びに第2の実施形態においては、アカマンボウ100の各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)の特徴を知るために、個別に抽出工程(ステップS3)及び分離工程(ステップS4)、並びに必要に応じた濃縮工程(ステップS5)、乾燥工程(ステップS6)、粉末化工程(ステップS7)、分級工程(ステップS8)、又は精製工程(ステップS9)が行われているが、本実施形態はそのような態様に限定されない。 <Other embodiments>
By the way, in 1st Embodiment and its each modification, and 2nd Embodiment, each site | part (the
例えば、表1に示すように、カルノシンを多く含むためにイミダゾールジペプチドの量が多い内臓部30と皮部40とを混合し得る状態となるように、切断(解体)工程(ステップS2)以降の各工程が実施されることも採用し得る一態様である。また、バレニンを含むイミダゾールジペプチドを豊富に含有するという、顕著な特徴を有する各部位(頭部10,普通筋20a,血合肉20b,内臓部30,皮部40)の全てを混合し得る状態となるように、切断(解体)工程(ステップS2)以降の各工程が実施されることも採用し得る一態様である。
For example, as shown in Table 1, in order to be able to mix the visceral part 30 and the skin part 40 with a large amount of imidazole dipeptide because they contain a lot of carnosine, the cutting (disassembly) step (step S2) and subsequent steps are performed. It is also an embodiment that can adopt each step. In addition, it is possible to mix all the parts (head 10, normal muscle 20a, blood meat 20b, internal organs 30, skin 40) having distinctive features of being rich in imidazole dipeptides containing valenine; It is one mode which can also adopt that each process after a cutting (disassembly) process (Step S2) is carried out so that it may become.
また、第1の実施形態及びその各変形例、並びに第2の実施形態においては、はえ縄漁船によって漁獲されたアカマンボウを、速やかに(例えば、60分以内)に漁船上において低温凍結処理(例えば、-65℃以上-15℃以下)を施したが、アカマンボウの漁獲方法、及びアカマンボウの漁船における保存方法は前述の例に限定されない。但し、イミダゾールジペプチド(代表的には、バレニン)の量を自己消化によって減少させる可能性を低減する観点から言えば、漁獲されたアカマンボウを、速やかに(例えば、60分以内)に漁船上において低温凍結処理(例えば、-65℃以上-15℃以下)することは、好適な一態様である。
Further, in the first embodiment and the modifications thereof, and the second embodiment, the red sea bream caught by the longline fishing boat is quickly frozen (for example, within 60 minutes) on the fishing boat at a low temperature freezing treatment (for example, However, the method for catching red sea bream and the method for storing red sea bream in a fishing boat are not limited to the above examples. However, from the viewpoint of reducing the possibility of reducing the amount of imidazole dipeptide (typically, valerine) by autolysis, the captured red squirrel is quickly (eg, within 60 minutes) on a fishing boat. A low-temperature freezing treatment (for example, −65 ° C. or more and −15 ° C. or less) is a preferable embodiment.
また、第1の実施形態においては、細片化されたアカマンボウ100の各部位が、該容器内の約60℃以上約100℃以下の抽出媒体(例えば、水)中に浸漬される抽出工程(ステップS3)が行われるが、第1の実施形態はそのような抽出工程に限定されない。例えば、次の(a)~(c)に示すような抽出工程(ステップS3)を採用することも、第1の実施形態の好適な変形例である。
(a)温度が20℃以上、30℃以上、40℃以上、又は50℃以上の抽出媒体(例えば、水)中に、細片化されたアカマンボウ100の各部位が浸漬される抽出工程
(b)抽出工程の該容器内の圧力が、通常採用される約1atm(約0.101MPa)とは異なる圧力(例えば、約0.001MPa以上約100MPa以下(但し、約0.101MPaを除く))である抽出工程
(c)抽出媒体が、生理学的に許容可能な液状媒体(例えば、有機液状媒体)、及び/又は他の生理学的に許容可能な液状媒体の例としての塩水である抽出工程
ここで、前述の「生理学的に許容可能な液状媒体」は、アルコール(代表的には、高純度のエタノール(例えば、99.5%、又は100%))に限定されない。例えば、ビール、ワイン、及び日本酒を含む醸造酒、ウィスキー、焼酎、及びウォッカを含む蒸留酒、並びに、カシス及びカンパリを含む混成酒を含み得る。なお、水が「生理学的に許容可能な液状媒体」に含まれることは言うまでもない。 Further, in the first embodiment, the extraction step in which each portion of the striped red sea bream 100 is immersed in an extraction medium (for example, water) of about 60 ° C. or more and about 100 ° C. or less in the container. (Step S3) is performed, but the first embodiment is not limited to such an extraction process. For example, adopting an extraction process (step S3) as shown in the following (a) to (c) is also a preferred modification of the first embodiment.
(A) Extraction step in which each part of the striped red sea bream 100 is immersed in an extraction medium (for example, water) having a temperature of 20 ° C. or higher, 30 ° C. or higher, 40 ° C. or higher, or 50 ° C. or higher. b) The pressure in the container of the extraction step is different from the normally employed about 1 atm (about 0.101 MPa) (for example, about 0.001 MPa to about 100 MPa (excluding about 0.101 MPa)) (C) an extraction step wherein the extraction medium is a physiologically acceptable liquid medium (eg, organic liquid medium) and / or salt water as an example of other physiologically acceptable liquid medium Thus, the aforementioned “physiologically acceptable liquid medium” is not limited to alcohol (typically, high-purity ethanol (eg, 99.5% or 100%)). For example, it can include beer, wine, and brewed liquors including sake, whiskey, shochu, and distilled liquor including vodka, and mixed liquor including cassis and campari. Needless to say, water is included in the “physiologically acceptable liquid medium”.
(a)温度が20℃以上、30℃以上、40℃以上、又は50℃以上の抽出媒体(例えば、水)中に、細片化されたアカマンボウ100の各部位が浸漬される抽出工程
(b)抽出工程の該容器内の圧力が、通常採用される約1atm(約0.101MPa)とは異なる圧力(例えば、約0.001MPa以上約100MPa以下(但し、約0.101MPaを除く))である抽出工程
(c)抽出媒体が、生理学的に許容可能な液状媒体(例えば、有機液状媒体)、及び/又は他の生理学的に許容可能な液状媒体の例としての塩水である抽出工程
ここで、前述の「生理学的に許容可能な液状媒体」は、アルコール(代表的には、高純度のエタノール(例えば、99.5%、又は100%))に限定されない。例えば、ビール、ワイン、及び日本酒を含む醸造酒、ウィスキー、焼酎、及びウォッカを含む蒸留酒、並びに、カシス及びカンパリを含む混成酒を含み得る。なお、水が「生理学的に許容可能な液状媒体」に含まれることは言うまでもない。 Further, in the first embodiment, the extraction step in which each portion of the striped red sea bream 100 is immersed in an extraction medium (for example, water) of about 60 ° C. or more and about 100 ° C. or less in the container. (Step S3) is performed, but the first embodiment is not limited to such an extraction process. For example, adopting an extraction process (step S3) as shown in the following (a) to (c) is also a preferred modification of the first embodiment.
(A) Extraction step in which each part of the striped red sea bream 100 is immersed in an extraction medium (for example, water) having a temperature of 20 ° C. or higher, 30 ° C. or higher, 40 ° C. or higher, or 50 ° C. or higher. b) The pressure in the container of the extraction step is different from the normally employed about 1 atm (about 0.101 MPa) (for example, about 0.001 MPa to about 100 MPa (excluding about 0.101 MPa)) (C) an extraction step wherein the extraction medium is a physiologically acceptable liquid medium (eg, organic liquid medium) and / or salt water as an example of other physiologically acceptable liquid medium Thus, the aforementioned “physiologically acceptable liquid medium” is not limited to alcohol (typically, high-purity ethanol (eg, 99.5% or 100%)). For example, it can include beer, wine, and brewed liquors including sake, whiskey, shochu, and distilled liquor including vodka, and mixed liquor including cassis and campari. Needless to say, water is included in the “physiologically acceptable liquid medium”.
なお、上述の第1の実施形態の変形例として説明した各抽出工程(ステップS3)のうち、(a)の抽出工程が採用された場合は、より低温による抽出が実現されるため、省エネルギーに寄与し得る。本発明者が調べた結果、通常採用される約1atm(約0.101MPa)下において、該抽出媒体の温度が20℃であっても、第1の実施形態の一例としての温度(約60℃)において抽出できる量を1としたときに約0.77を抽出し得るという知見を得ている。
Of the extraction steps (step S3) described as a modification of the first embodiment described above, when the extraction step (a) is adopted, extraction at a lower temperature is realized, thus saving energy. Can contribute. As a result of investigation by the present inventor, even if the temperature of the extraction medium is 20 ° C. under a normally employed about 1 atm (about 0.101 MPa), the temperature as an example of the first embodiment (about 60 ° C. In this case, it has been found that about 0.77 can be extracted when the amount that can be extracted is 1).
上述の内容を、より具体的なデータに基づいて説明する。図4は、第1の実施形態の抽出工程において、温度が20℃~60℃の水を用いて抽出したときの、普通筋20aにおけるバレニンの量(mg/100g)(図4の点線)と、温度が60℃の水を用いて抽出されたバレニンの量を1としたときの、20℃~50℃の水を用いて抽出されたバレニンの量の割合(図4の実線)を示すグラフである。なお、バレニンの量の分析方法は、第1の実施形態において説明された方法と同様である。
The above contents will be explained based on more specific data. FIG. 4 shows the amount of barenine in the normal muscle 20a (mg / 100 g) (dotted line in FIG. 4) when extracted using water having a temperature of 20 ° C. to 60 ° C. in the extraction step of the first embodiment. FIG. 4 is a graph showing the ratio of the amount of valenine extracted using water at 20 ° C. to 50 ° C. when the amount of valenine extracted using water at a temperature of 60 ° C. is 1 (solid line in FIG. 4). It is. The method for analyzing the amount of valenin is the same as the method described in the first embodiment.
図4に示すように、20℃以上の抽出媒体(例えば、水)を採用することにより、60℃の抽出媒体(例えば、水)の場合と比較しても遜色ない程度のバレニンの量(75%以上)を得ることが可能であることを確認することができた。なお、20℃という、抽出温度としてはかなり低温の抽出媒体であっても、上述のとおり相当量のイミダゾールジペプチド(代表的には、バレニン)を抽出し得ることは、特筆に値する。
As shown in FIG. 4, by employing an extraction medium (for example, water) of 20 ° C. or higher, the amount of valenin (75) that is comparable to that of an extraction medium (for example, water) at 60 ° C. % Or more) can be confirmed. In addition, it is worthy of special mention that a considerable amount of imidazole dipeptide (typically, valenin) can be extracted as described above even with an extraction medium having an extraction temperature of 20 ° C. which is considerably low.
また、上述の第1の実施形態の変形例として説明した各抽出工程(ステップS3)のうち、(b)の抽出工程が採用された場合は、例えば、通常採用される圧力よりも高い圧力によって抽出される場合は、より低温の抽出媒体を用いて抽出工程を実現し得る。
Moreover, when the extraction process of (b) is employ | adopted among each extraction process (step S3) demonstrated as a modification of the above-mentioned 1st Embodiment, for example by the pressure higher than the pressure normally employ | adopted When extracted, the extraction process can be realized using a lower temperature extraction medium.
また、上述の第1の実施形態の変形例として説明した各抽出工程(ステップS3)のうち、(c)の抽出工程が採用された場合は、抽出物の風味を向上させることに寄与し得る。例えば、エタノール(純度99.5%)を用いて上述の(c)の抽出工程が行われた場合のイミダゾールジペプチド(代表的には、バレニン)の量は、水を抽出媒体とした場合のイミダゾールジペプチド(代表的には、バレニン)の量の約70%であることが確認されている。従って、抽出媒体がアルコールである場合は、抽出媒体が水である場合よりも抽出量が減少するが、水の場合の抽出量の約70%であっても、相当量のイミダゾールジペプチド(代表的には、バレニン)が抽出されることは特筆に値する。従って、水以外の抽出媒体が採用された場合であっても、第1の実施形態の少なくとも一部の効果が奏され得る。
Moreover, when the extraction process of (c) is employ | adopted among each extraction process (step S3) demonstrated as a modification of the above-mentioned 1st Embodiment, it can contribute to improving the flavor of an extract. . For example, the amount of imidazole dipeptide (typically valenin) when the extraction step (c) described above is performed using ethanol (purity 99.5%) is the imidazole when water is used as the extraction medium. It has been confirmed to be about 70% of the amount of dipeptide (typically valenin). Therefore, when the extraction medium is alcohol, the extraction amount is reduced compared to when the extraction medium is water, but even if it is about 70% of the extraction amount in the case of water, a considerable amount of imidazole dipeptide (typically It is worth mentioning that valenin is extracted. Therefore, even when an extraction medium other than water is employed, at least some of the effects of the first embodiment can be achieved.
また、第1の実施形態及びその各変形例(1)~(3)、第2の実施形態、並びにその他の実施形態においては、アカマンボウ100の背びれ又は尾ひれ90が生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物(代表的には水溶性抽出物であるが、水溶性抽出物に限定されない。また、濃縮抽出物及び乾燥抽出物を含む。以下、同じ。)に含まれていないが、該抽出物は、そのような態様に限定されない。例えば、該抽出物の製造工程をより簡便化するために、図2におけるC3に示される切断を行わずに、その後の各工程が行われることも、採用し得る一態様である。従って、背びれ及び/又は尾ひれ90が、第1の実施形態及びその各変形例(1)~(3)、並びに第2の実施形態の抽出物の構成成分の一つとして含まれることも採用され得る。
In the first embodiment and its modifications (1) to (3), the second embodiment, and other embodiments, the dorsal fin or tail fin 90 of the red sea bream 100 is a physiologically acceptable liquid. Extracts extracted using a medium soluble or physiologically acceptable liquid medium as an extraction medium (typically a water-soluble extract, but not limited to a water-soluble extract. The extract is not limited to such an embodiment, although it is not included in the following. For example, in order to further simplify the manufacturing process of the extract, without cutting shown in C 3 in FIG. 2, it is an aspect that may be employed for each subsequent step. Therefore, it is also adopted that the dorsal fin and / or tail fin 90 is included as one of the constituent components of the extract of the first embodiment and its modifications (1) to (3) and the second embodiment. obtain.
一方、表1に示すように、血合肉20bが含有するイミダゾールジペプチド又はバレニンの量のバラつきは大きい。従って、より安定した量のイミダゾールジペプチド又はバレニンを含有する、生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を得る観点から言えば、上述のように各部位が混合される場合には、混合される血合肉20bの量が5wt%未満であることが好ましい。また、別の観点から言えば、第1の実施形態及びその各変形例(1)~(3)、並びに第2の実施形態の該抽出物について、血合肉から形成された、アカマンボウ由来の生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物の割合が5wt%未満であることが、より安定した量のイミダゾールジペプチド又はバレニンを含有する該抽出物の製造を実現し得る。
On the other hand, as shown in Table 1, the amount of imidazole dipeptide or valenin contained in the blood meat 20b varies greatly. Therefore, it can be said from the viewpoint of obtaining an extract which contains a more stable amount of imidazole dipeptide or valenine and is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium. For example, when each part is mixed as described above, the amount of the mixed blood 20b to be mixed is preferably less than 5 wt%. From another point of view, the first embodiment and its modifications (1) to (3) and the extract of the second embodiment are derived from red sea cucumber and formed from bloody meat. It is more stable amount of imidazole dipeptide or valenine that the ratio of the extract which is soluble in a physiologically acceptable liquid medium or is extracted using a physiologically acceptable liquid medium as an extraction medium is less than 5 wt% The production of the extract containing can be realized.
さらに、第1の実施形態及びその各変形例(1)~(3)、第2の実施形態、並びにその他の実施形態において製造された、生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を構成成分の一部として含む、錠剤、カプセル剤、散剤(顆粒剤を含む)、丸剤、シロップ剤、液剤、ドリンク剤、トローチ剤、ドロップ、水飴等(以下、総称して「製剤」という。)を製造することは、採用し得る好適な一態様である。該製剤は、イミダゾールジペプチド、特に、非常に豊富な量のバレニンを含有しているため、該製剤を摂取することにより、例えば抗酸化作用及び/又は抗疲労作用が奏され得る。なお、該製剤は、公知の製造方法によって製造され得る。また、該製剤は、成形性の向上又は経口投与するときの容易性の向上等のため、適宜、賦形剤、結合剤、崩壊剤、又は湿潤剤、あるいは蜂蜜又は米粉等を混合することによって形成され得る。
Furthermore, it is soluble or physiological in a physiologically acceptable liquid medium manufactured in the first embodiment and its modifications (1) to (3), the second embodiment, and other embodiments. Tablets, capsules, powders (including granules), pills, syrups, liquids, drinks, lozenges containing extracts that are extracted using a liquid medium that is acceptable as an extraction medium Producing agents, drops, chickenpox and the like (hereinafter collectively referred to as “formulations”) is a preferred embodiment that can be employed. Since the preparation contains an imidazole dipeptide, in particular, a very abundant amount of valenin, for example, an antioxidant action and / or an anti-fatigue action can be achieved by taking the preparation. In addition, this formulation can be manufactured by a well-known manufacturing method. In addition, the preparation may be mixed with excipients, binders, disintegrants, wetting agents, honey or rice flour, etc., as appropriate, in order to improve moldability or ease of oral administration. Can be formed.
本発明の1つの生理学的に許容可能な液状媒体に可溶な又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物及びその製造方法、並びに剤形は、バレニンを豊富に含み得る魚由来の該抽出物及びその製造方法であるため、食品業及び水産業に限らず、医薬、健康、医療、美容に関連する各産業においても極めて有用である。
The extract which is soluble in one physiologically acceptable liquid medium of the present invention or is extracted using a physiologically acceptable liquid medium as an extraction medium, a method for producing the same, and a dosage form are rich in valenin. Since it is the fish-derived extract obtained and the method for producing the same, it is extremely useful not only in the food industry and the fishery industry but also in various industries related to medicine, health, medical care, and beauty.
10 頭部
20 筋肉
20a 普通筋
20b 血合肉
30 内臓部
90 尾ひれ
100 アカマンボウ 10head 20 muscle 20a normal muscle 20b blood mixed meat 30 internal organs 90 tail fin 100 red sea bream
20 筋肉
20a 普通筋
20b 血合肉
30 内臓部
90 尾ひれ
100 アカマンボウ 10
Claims (16)
- アカマンボウ由来であり、かつ
生理学的に許容可能な液状媒体に可溶な、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される、
抽出物。 It is derived from a red sea cucumber and is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium.
Extract. - バレニンを7wt%以上含有する、
請求項1に記載の抽出物。 Contains 7 wt% or more of barenine,
The extract according to claim 1. - バレニンを10wt%以上含有する、
請求項1に記載の抽出物。 Containing 10 wt% or more of barenine,
The extract according to claim 1. - さらに、イミダゾールジペプチドを25wt%以上含有する、
請求項1乃至請求項3のいずれか1項に記載の抽出物。 Furthermore, containing imidazole dipeptide 25 wt% or more,
The extract according to any one of claims 1 to 3. - 前記イミダゾールジペプチド(但し、バレニンを含む)の含有量を1としたときの、前記バレニンの含有量が、0.5以上0.97以下である、
請求項4に記載の抽出物。 When the content of the imidazole dipeptide (including valenin) is 1, the content of the valenin is 0.5 or more and 0.97 or less.
The extract according to claim 4. - 精製されていない、
請求項1乃至請求項5のいずれか1項に記載の抽出物。 Not purified,
The extract according to any one of claims 1 to 5. - 血合肉から形成された、前記アカマンボウ由来の前記抽出物の割合が5wt%未満である、
請求項1乃至請求項6のいずれか1項に記載の抽出物。 The proportion of the extract derived from the red sea cucumber formed from the bloody meat is less than 5 wt%,
The extract according to any one of claims 1 to 6. - 水分量が0wt%超10wt%以下の粉体である、
請求項1乃至請求項7のいずれか1項に記載の抽出物。 It is a powder having a moisture content of more than 0 wt% and not more than 10 wt%.
The extract according to any one of claims 1 to 7. - 請求項1乃至請求項8のいずれか1項に記載の抽出物を含む、錠剤、カプセル剤、散剤、丸剤、シロップ剤、液剤、ドリンク剤、トローチ剤、ドロップ、又は水飴である、
製剤。 A tablet, a capsule, a powder, a pill, a syrup, a liquid, a drink, a troche, a drop, or a chickenpox, comprising the extract according to any one of claims 1 to 8.
Formulation. - アカマンボウを20℃以上の抽出媒体に接触させることにより、生理学的に許容可能な液状媒体に可溶な抽出物、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を抽出する、抽出工程を含む、
抽出物の製造方法。 By bringing the red squirrel into contact with an extraction medium at 20 ° C. or higher, an extract that is soluble in a physiologically acceptable liquid medium or an extract that is extracted using a physiologically acceptable liquid medium as an extraction medium is extracted. Including an extraction step,
A method for producing an extract. - アカマンボウを60℃以上の抽出媒体に接触させることにより、生理学的に許容可能な液状媒体に可溶な抽出物、又は生理学的に許容可能な液状媒体を抽出媒体として抽出される抽出物を抽出する、抽出工程を含む、
抽出物の製造方法。 Extracting extract that is soluble in a physiologically acceptable liquid medium or extracted using a physiologically acceptable liquid medium as an extraction medium by bringing the red bowfish into contact with an extraction medium at 60 ° C. or higher Including an extraction step,
A method for producing an extract. - 前記抽出工程の後に、前記抽出物を濃縮し、バレニンを5wt%以上含有する濃縮抽出物を得る濃縮工程と、を含む、
請求項10又は請求項11に記載の抽出物の製造方法。 A step of concentrating the extract after the extraction step to obtain a concentrated extract containing 5 wt% or more of valenin.
The manufacturing method of the extract of Claim 10 or Claim 11. - 前記濃縮工程の後に、前記抽出物の水分量が0wt%超10wt%以下になるように前記抽出物を乾燥し、バレニンを7wt%以上含有する乾燥抽出物を得る乾燥工程を、さらに含む、
請求項12に記載の抽出物の製造方法。 The method further includes, after the concentration step, a drying step of drying the extract so that the water content of the extract is more than 0 wt% and 10 wt% or less to obtain a dry extract containing 7 wt% or more of valenin.
The manufacturing method of the extract of Claim 12. - 前記乾燥抽出物を粉砕して、1mm未満の粒子径を有する前記乾燥抽出物の粉体を得る、粉末化工程を、さらに含む、
請求項13に記載の抽出物の製造方法。 Pulverizing the dried extract to obtain a powder of the dried extract having a particle size of less than 1 mm, further comprising a powdering step
A method for producing the extract according to claim 13. - 前記バレニンを含むイミダゾールジペプチドを精製する精製工程を、さらに含む、
請求項10乃至請求項12のいずれか1項に記載の抽出物の製造方法。 Further comprising a purification step of purifying the imidazole dipeptide containing the valenin.
The method for producing an extract according to any one of claims 10 to 12. - 血合肉から形成された、前記アカマンボウ由来の前記抽出物の割合が5wt%未満である、
請求項10乃至請求項15のいずれか1項に記載の抽出物の製造方法。 The proportion of the extract derived from the red sea cucumber formed from the bloody meat is less than 5 wt%,
The method for producing an extract according to any one of claims 10 to 15.
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Non-Patent Citations (2)
Title |
---|
ANONYMOUS: "How to prepare, how to eat", BOUZ-KONNYAKU'S COMMERCIAL GUIDE TO FISH AND SELLFISH. AKAMANBO, SUNFISH, 2007, XP055634417, Retrieved from the Internet <URL:https://www.zukan-bouz.com/syu/%E3%82%A2%E3%82%AB%E3%83%9E%E3%83%B3%E3%83%9C%E3%82%A6> [retrieved on 20180530] * |
OMURA YUJI ET AL.: "Amounts of balenine in Akamanbo (Lampris Guttatus) meat", 2018 JSFS SPRING MEETING PROCEEDINGS, 26 March 2018 (2018-03-26), pages 92 * |
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