Method for producing oyster meat essence containing large amount of antioxidants having high antioxidative power and high ORAC value

Abstract

To provide a method for producing an oyster meat essence that more amply incorporates an antioxidant substance with high ORAC value as follows. A portion of an oyster meat extract more amply incorporating an antioxidant substance with high ORAC value is selected. An extraction method that allows incorporating further large amount of antioxidant substance with high ORAC value is employed. The beneficial oyster meat extract can be efficiently extracted in large amounts. Object An oyster meat is stored in an extraction container where water is accumulated. An oyster meat essence is extracted to generate an extract liquid. The extract liquid is injected to a centrifuge, and concurrently the centrifuge is rotated at a centrifugal acceleration where an antioxidant substance with high antioxidative potency and ORAC value is separated and removed from the extract liquid. The antioxidant substance with higher antioxidative potency and ORAC value is separated. Thus, the oyster meat essence incorporating a large amount of antioxidant substance with high antioxidative potency and ORAC value is obtained.

Claims

1. A method for producing an oyster meat product with high antioxidative potency, consisting essentially of: (a) storing an oyster meat in an extraction container where a water solution is accumulated, (b) extracting liquid from the oyster meat in the extraction container to generate an extract liquid, (c) removing the oyster meat from the extraction container after the extraction, (d) concentrating the extract liquid after the removal of the oyster meat to generate a concentration liquid, (e) adding ethanol to the concentration liquid, (f) separating the concentration liquid into a precipitate and a first supernatant, (g) removing the first supernatant after the separation, (h) injecting the first supernatant together with the ethanol to a continuous centrifuge, (i) rotating the continuous centrifuge at a rotation speed which applies a centrifugal acceleration to the first supernatant, wherein the first supernatant is separated into a second supernatant and a centrifugation precipitate, and (j) removing the second supernatant from the continuous centrifuge, to obtain the oyster meat product with high antioxidative potency.

2. The method according to claim 1, wherein step (b) is performed using hot water at a temperature of 30 to 50 C.

3. The method according to claim 1, wherein step (f) is performed using natural sedimentation with or without stirring.

4. The method according to claim 1, wherein ethanol is added to the concentration liquid in step (e) to obtain a concentration liquid having an ethanol concentration of 30 to 80%.

5. The method according to claim 1, wherein ethanol is added to the concentration liquid in step (e) to obtain a concentration liquid having an ethanol concentration of 70 to 80%.

6. A method for producing an oyster meat product with high antioxidative potency, consisting of: (a) storing an oyster meat in an extraction container where a water solution is accumulated, (b) extracting liquid from the oyster meat in the extraction container to generate an extract liquid, (c) removing the oyster meat from the extraction container after the extraction, (d) concentrating the extract liquid after the removal of the oyster meat to generate a concentration liquid, (e) adding ethanol to the concentration liquid, (f) separating the concentration liquid into a precipitate and a first supernatant, (g) removing the first supernatant after the separation, (h) injecting the first supernatant together with the ethanol to a continuous centrifuge, (i) rotating the continuous centrifuge at a rotation speed which applies a centrifugal acceleration to the first supernatant, wherein the first supernatant is separated into a second supernatant and a centrifugation precipitate, and (j) removing the second supernatant from the continuous centrifuge, to obtain the oyster meat product with high antioxidative potency.

7. The method according to claim 6, wherein step (b) is performed using hot water at a temperature of 30 to 50 C.

8. The method according to claim 6, wherein step (f) is performed using natural sedimentation with or without stirring.

9. The method according to claim 6, wherein ethanol is added to the concentration liquid in step (e) to obtain a concentration liquid having an ethanol concentration of 30 to 80%.

10. The method according to claim 6, wherein ethanol is added to the concentration liquid in step (e) to obtain a concentration liquid having an ethanol concentration of 70 to 80%.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) FIG. 1 is an explanatory view of a schematic configuration illustrating a method for producing an oyster meat essence incorporating a large amount of antioxidant substance with a high antioxidative potency and ORAC value according to the present invention (first);

(2) FIG. 2 is an explanatory view illustrating a schematic configuration of a continuous centrifuge according to the present invention;

(3) FIG. 3 is an explanatory view illustrating a schematic configuration of the continuous centrifuge according to another embodiment;

(4) FIG. 4 is an explanatory view illustrating a measurement principle of an ORAC method;

(5) FIG. 5 is an explanatory view illustrating a calculation method of an ORAC value and an apparatus, a reagent, and a unit used for the ORAC method;

(6) FIG. 6 is an explanatory view illustrating ORAC values of various food products;

(7) FIG. 7 is an explanatory view illustrating a calculation example of a maximum centrifugal acceleration;

(8) FIG. 8 is an explanatory view of a schematic configuration illustrating a method for producing the oyster meat essence incorporating a large amount of antioxidant substance with a high ORAC value according to a second embodiment of the present invention;

(9) FIG. 9 is a flowchart illustrating the method for producing the oyster meat essence incorporating a large amount of antioxidant substance with a high ORAC value according to the second embodiment of the present invention (first);

(10) FIG. 10 is a flowchart illustrating the method for producing the oyster meat essence incorporating a large amount of antioxidant substance with a high ORAC value according to the second embodiment of the present invention (second);

(11) FIG. 11 is an explanatory view illustrating the schematic configuration of the continuous centrifuge according to the second embodiment of the present invention; and

(12) FIG. 12 is an explanatory view illustrating ORAC values of various food products in the second embodiment.

BEST MODE FOR CARRYING OUT THE INVENTION

(13) A preferred embodiment of the present invention will be described below.

Working Example 1

(14) First, as illustrated in FIG. 1, to extract an oyster meat essence, an oyster meat 3 is stored in an extraction container 2 accumulating water 1.

(15) Here, the kind of the water 1 used for the extraction is not limited. Generally, water may be used. The temperature of this water is not also limited. The water may be at a general normal temperature, may be warm water at 30 C. to 50 C., or may be hot water equal to or more than 50 C. Ethanol may be mixed with the water to create an ethanol solution. Mixing ethanol in water promotes the extraction of the oyster meat essence in the ethanol solution.

(16) In the extraction, the inside of the extraction container 2 may be at normal pressure, or the inside of the extraction container 2 may be sealed, and the pressure may be reduced to equal to or less than 1 atmosphere or the pressure may be increased to equal to or more than 1 atmosphere.

(17) This is to select a good extraction method that allows incorporating a large amount of antioxidant substance with a high antioxidative potency.

(18) Next, after a lapse of a predetermined period, for example, after a lapse of extraction period of several hours, the oyster meat 3 is removed from the inside of the extraction container 2, and the extracted extract liquid in the extraction container 2 is concentrated, thus concentration liquid 4 is created.

(19) Various concentration methods are also available for this concentration method. The concentration method is not limited in the present invention, and any concentration method is applicable. A so-called low-temperature heating condensation method and a high-temperature heating condensation method are applicable.

(20) The concentration ratio of the concentration liquid 4 is not also limited. The concentration liquid 4 may be concentrated to one third or half.

(21) Next, ethanol 5 is added to the concentration liquid 4 so that the ethanol concentration may be about 30% to 80%, preferably, the ethanol concentration may be 70%. The concentration liquid 4 where the ethanol 5 has been added and attenuated is stirred and separated into a precipitate 6 and a supernatant 7. This separation method is not limited. However, in a natural separation method by means of natural sedimentation, after the solution is stirred, it is left as it is for a predetermined period of time to await the precipitate 6 precipitating naturally.

(22) After the precipitate 6 precipitates and the precipitate 6 and the supernatant 7 are completely separated, only this supernatant 7 is removed.

(23) It is constituted so that this supernatant 7 can be continuously injected from an injection pipe 9 of a continuous centrifuge 8 illustrated in FIG. 2 to the inside of the continuous centrifuge 8. As shown in FIG. 3, the supernatant 7 may be injected from an injection pipe 10 on the left side while the ethanol 5 may be injected from an injection pipe 11 on the right side. The action of the ethanol 5 promotes the centrifugation action of the continuous centrifuge 8 for further separation.

(24) Here, the injection of the predetermined amount of the supernatant 7 to the inside of the continuous centrifuge 8 is confirmed, and the continuous centrifuge 8 operates. Thus, the supernatant 7 is continuously separated into a so-called centrifugation precipitate 15 and a centrifugation supernatant 16.

(25) As seen from FIG. 2 and FIG. 3, the so-called centrifugation precipitate 15 is collected to an outer periphery sidewall 13 side of a storage tank 12 by a centrifugal force. Apart from that, the so-called centrifugation supernatant 16 is delivered from upward of the storage tank 12 to the outside via a delivery pipe 14.

(26) In this working example, as seen from FIG. 1, for example, the concentration liquid 4 where the ethanol 5 had been added so that the concentration liquid 4 may become the concentration of 70% was stirred, and then it was left to await the concentration liquid 4 to precipitating naturally. The supernatant 7 extracted after the natural precipitation of, for example, 30 liters, was continuously injected to the continuous centrifuge 8.

(27) The continuous centrifuge 8 was operated, thus centrifugation was continuously performed on the supernatant 7.

(28) As a result, it was confirmed that the so-called centrifugation precipitate 15 of 0.3 liters and the continuous centrifugation supernatant 16 of 29.7 liters were extracted.

(29) In the present invention, it was able to be confirmed that the continuous centrifugation supernatant 16 incorporated a large amount of antioxidant substance with a high antioxidative potency and ORAC value.

(30) Here, to what extent of substances with antioxidative potency were contained in the centrifugation supernatant 16 was examined by a so-called Oxygen Radical Absorbance Capacity method (an ORAC method). By the ORAC method, a value indicating the antioxidative potency, namely, an ORAC value was detected. Consequently, as described above, it was confirmed that the centrifugation supernatant 16 incorporated the antioxidant substance with extremely high antioxidative potency and ORAC value.

(31) Now, the measurement principle of the ORAC method will be somewhat described. First, in the case where constant reactive oxygen species are generated, the fluorescence intensity degraded by the reactive oxygen species is measured, and the curve of the fluorescence intensity decreasing over time is depicted, the rate of decrease in the fluorescence intensity of the fluorescent substance is delayed by coexistence of the antioxidant substance with the reaction system. Accordingly, with this principle, the presence of the antioxidant substance can be confirmed.

(32) Based on the principles, a description will be given with reference to FIG. 4. The difference between the Area Under the Curve (AUC) of the fluorescence intensity under the presence of a sample or a standard substance, and the AUC under their absence (blank) is calculated (the net AUC). Regarding the net AUC for the sample, a relative value with respect to the net AUC of a standard substance (Trolox) of known concentration to is found. The relative value is as a base converted into Trolox concentration, and taken as the antioxidative potency of the sample (unitsmol TE/g: micromoles Trolox-equivalent/gram).

(33) The calculation method of the ORAC value will be illustrated in FIG. 5.

(34) That is, in the ORAC method, first, a fluorescent probe (Fluorescein) is added to a sample solution or a standard solution (Trolox), and activation oxygen is generated using AAPH (2,2-Azobis(2-amidinopropane) dihydrochloride) as a radical initiator. This oxidizes the Fluorescein by the reactive oxygen.

(35) Since the oxidized Fluorescein does not exhibit fluorescence, the fluorescence intensity is reduced over time. If the sample exhibits antioxidative potency, the reactive oxygen is removed by the antioxidant substance, and the oxidation of the Fluorescein is suppressed. Accordingly, the fluorescence intensity of the Fluorescein is maintained and the reduction speed is delayed compared with the case where the antioxidant substance is absent (blank).

(36) The fluorescence intensity of the sample or of Trolox, and of the blank are plotted on the vertical axis while the measurement period is plotted on the horizontal axis. The difference between the Area Under the Curve of the fluorescence intensity of the sample solution or of Trolox (AUCsample or AUCTrolox), and the Area Under the Curve of the blank (AUCblank), that is, the area of the diagonal-hatching section, is calculated (each respectively referred to as netAUCsample and netAUCTrolox). The Trolox concentration equivalent to netAUCsample for the sample is found from netAUCTrolox for the standard substance. The ORAC value is calculated, for example, as the number of micromoles of Trolox per gram of the sample.

(37) Accordingly, for example, mole TE/g (TE: Trolox-Equivalent) is employed as the unit of the ORAC value.

(38) Here, the ORAC value is expressed by converting the antioxidative potency into the amount of standard substance (Trolox). It should be noted that the ORAC value is not a value indicating a specific weight of antioxidative substance. However, if the ORAC value is high, for example, it can be seen that the oyster meat essence incorporates an antioxidant substance with a high antioxidative potency.

(39) In this working example, the ORAC value of the continuous centrifugation supernatant 16 was detected. The detected value was 160 mole TE/g, which was extremely high value among usual food groups.

(40) ORAC Company in the United States of America makes a database of ORAC values of various food products. The graph of the ORAC values is illustrated in FIG. 6. As seen from FIG. 6, even a blueberry, which is recognized as having a high ORAC value by ORAC Company in the United States of America, the ORAC value is 66.2 mole TE/g.

(41) In contrast to this, it can be seen that the oyster meat essence of this working example, namely, the continuous centrifugation supernatant 16 incorporates an antioxidant substance with the ORAC value of 160 mole TE/g, which is a value regarded as having high antioxidative potency and ORAC value approximately double the ORAC value of the blueberry.

(42) The inventors of the present invention added the ethanol 5 to the oyster meat essence before being separated by the continuous centrifuge 8 in the present invention, namely, the concentration liquid 4 of the extract liquid as illustrated in FIG. 1. Then, the ORAC value of the solution, which had become an ethanol solution with a concentration of 70%, for example, was also detected. As a result, the ORAC value of 132 mole TE/g was detected from the solution that had become the ethanol solution with a concentration of 70%.

(43) As described above, the liquid of 30 liters made as the ethanol solution was centrifuged by the continuous centrifuge 8 as described above to separate the liquid into the centrifugation supernatant 16 of 29.7 liters and the centrifugation precipitate 15 of 0.3 liters. Then, the ORAC value of the continuous centrifugation supernatant 16 indicated a high value, 160 mole TE/g, as described above. On the contrary, the ORAC value of the continuous centrifugation precipitate 15 indicated 30.7 mole TE/g.

(44) The reason for this is considered as follows. The continuous centrifuge 8 is rotated with strong rotational force, and centrifugal acceleration of equal to or more than the usual gravitation is applied to the injected supernatant 7.

(45) As a result, forcible separation is performed with the centrifugal acceleration. Accordingly, substances that are never separated and precipitated by the natural precipitation, that is, a substance without the antioxidative potency of the antioxidant substance and a substance with low antioxidative potency are considered to be forcibly separated. These substances are understood to be included in the continuous centrifugation precipitate 15 with the strong centrifugal acceleration.

(46) That is, the centrifugal acceleration by the rotation of the continuous centrifuge 8 exceeds a diffusion force where so-called fine particles, which do not precipitate only by the usual gravitation such as gravitation in natural precipitation, for example, the substance without the antioxidative potency of the antioxidant substance or the substance with low antioxidative potency, try to diffuse. Thus, the substance without the antioxidative potency of the antioxidant substance or the substance with low antioxidative potency, for example, is forcibly separated to the centrifugation precipitate 15 side.

(47) This is because of the following reasons. By operating and rotating the continuous centrifuge 8, the centrifugal acceleration is acted on the supernatant 7 injected in the storage tank 12. When this centrifugal acceleration becomes larger than the diffusion force where, for example, the substance without the antioxidative potency of the antioxidant substance or the substance with low antioxidative potency attempts to diffuses, these substances that do not precipitate in the natural precipitation are also separated. Thus, the centrifugation precipitate 15 is formed.

(48) Accordingly, the ORAC value before separation by the continuous centrifuge, a so-called solution of the concentration liquid where ethanol had been added, was 132 mole TE/g. Meanwhile, the ORAC value of the supernatant generated by forcible separation with the continuous centrifuge was 160 mole TE/g, which is an extremely high value. This allows extracting, obtaining, and producing an oyster meat essence with a large amount of antioxidant substance with extremely high antioxidative potency.

(49) The rotation speed of the continuous centrifuge 8 where the centrifugal acceleration exceeding the diffusion force of, for example, the substance without the antioxidative potency of the antioxidant substance or the substance with low antioxidative potency present in the supernatant 7 can be obtained will be considered. As seen from FIG. 7, assume that the maximum rotation radius of the continuous centrifuge 8 is 11.4 cm and the maximum rotation speed of the continuous centrifuge 8 is 8000 rpm. Then, the maximum centrifugal acceleration is a value of approximately 8157g.

(50) Therefore, in the present invention, the maximum centrifugal acceleration of the continuous centrifuge 8 had a value of approximately 8157g. It has been proved that the centrifugal acceleration around this value exceeds the diffusion force of a hindrance (particle) that inhibits the antioxidative potency of the antioxidant substance present in the supernatant 7.

Working Example 2

(51) Next, the working example 2 according to the present invention will be described with reference to FIG. 8 to FIG. 12. First, to extract an oyster meat essence, the oyster meat 3 is stored in the extraction container 2 accumulating the water 1.

(52) Here, the kind of the water 1 used for the extraction is not limited similarly to the working example 1. Generally, water may be used. The temperature of this water is not also limited. The water may be at a normal temperature, may be warm water around 30 C. to 50 C., or may be hot water equal to or more than 50 C. The ethanol 5 may be mixed with the water to use an ethanol solution. Mixing ethanol in water promotes the extraction of the oyster meat essence in the ethanol solution.

(53) In the extraction, the inside of the extraction container 2 may be at normal pressure, or the inside of the extraction container 2 may be sealed and the pressure may be reduced to equal to or less than 1 atmosphere or the pressure may be increased to equal to or more than 1 atmosphere.

(54) This is to examine and select a method for extracting a substance incorporating a large amount of antioxidant substance with a high antioxidative potency, namely, a high ORAC value described below.

(55) Next, after a lapse of a predetermined period, for example, after a lapse of extraction period of several hours, the oyster meat 3 is removed from the inside of the extraction container 2. After the removal, the extracted extract liquid in the extraction container 2 is concentrated, thus the first concentration liquid 4 is created.

(56) Various concentration methods are also available as the concentration method of this first concentration liquid 4. The concentration method is not limited in the present invention, and any method is applicable. A so-called low-temperature heating condensation method and a high-temperature heating condensation method are applicable.

(57) The concentration ratio of the first concentration liquid 4 is not also limited. The concentration liquid 4 may be concentrated to one third or half.

(58) Next, the ethanol 5 is added to the first concentration liquid 4 so that the ethanol concentration may be about 30% to 90%, preferably, the ethanol concentration may be 70%. Consequently, the first concentration liquid 4 attenuated by the added ethanol 5 is stirred and separated into the precipitate 6 and the first supernatant 7.

(59) This separation method is also not limited. However, in a natural separation method by means of natural sedimentation, after the solution is stirred, it is left as it is for a predetermined period of time to await the precipitate 6 precipitating naturally.

(60) In this working example, the ORAC values of the precipitate 6 and the first supernatant 7 in this step were measured. The ORAC value per gram of the precipitate 6 was only 12.32 mol TE/g: micromoles Trolox-equivalent/gram. The ORAC value per gram of the first supernatant 7 was 66 mol TE/g: micromoles Trolox-equivalent/gram.

(61) Thus, it is understood that in the liquid before the centrifugation described below, especially in the precipitate 6, the antioxidant substance with a high ORAC value was not separated. It is also understood that the antioxidant substance with a high ORAC value was not separated to exist in the first supernatant 7.

(62) However, by repeatedly performing the processes such as centrifugation, shaking, and centrifugation on the first supernatant 7, a second, a third, and a fourth supernatants were generated. This allowed extracting an antioxidant substance with a high ORAC value into, for example, the second, the third, and the fourth supernatants.

(63) Here, after the first supernatant 7 is removed, the first supernatant 7 is centrifuged with, for example, the continuous centrifuge to separate the first supernatant 7 into the precipitate 6 and a second supernatant 17.

(64) The flowcharts of FIG. 9 and FIG. 10 describe steps of after the second supernatant 17 is removed to the generation of the oyster meat essence including the antioxidant substance with a high ORAC value.

(65) First, the first supernatant 7 is centrifuged (see FIG. 8), and then the precipitate 6 and the second supernatant 17 are separated. Only this second supernatant 17 was removed (Step 100).

(66) The first concentration liquid 4 attenuated to a predetermined ethanol concentration, for example, the ethanol concentration of 70% by adding the ethanol 5 may be constituted as follows. The first concentration liquid 4 is put into the continuous centrifuge from the beginning, continuously centrifuged, and continuously separated into the precipitate 6 and the first supernatant 7 to obtain a large amount of the first supernatant 7.

(67) When the second supernatant 17 obtained as described above was an amount of, for example, 600 grams, this 600 grams of the second supernatant 17 was concentrated and a second concentration liquid 20 was created so as to be a water content rate of approximately 30% (Step 102).

(68) Here, this concentration operation of the second concentration liquid 20 is possibly performed by, for example, a rotary evaporator or a reduced-pressure concentration kneader. However, the concentration operation is not limited to this.

(69) The second concentration liquid 20 was concentrated so as to be the water content rate of approximately 30% and the amount of created second concentration liquid 20 became from 600 grams to approximately 157 grams by the concentration operation. Then, the water content rate was measured. The water content rate was approximately 33.3%.

(70) Here, the ORAC value of the second concentration liquid 20 of 157 grams was measured, and the ORAC value was measured. Even in this step, the ORAC value indicated 290 mol TE/g: micromoles Trolox-equivalent/gram, which is extremely high value. As described above, the ORAC value of the first supernatant 7 per gram was only 66 mol TE/g: micromoles Trolox-equivalent/gram.

(71) Next, for example, the ethanol of 240 grams with purity of 99.99% was added so that the ethanol concentration of the second concentration liquid 20 of 157 grams became, for example, approximately 80% as the entire solution. Thus, the ethanol solution with the ethanol concentration of approximately 80% was created.

(72) That is, the ethanol 5 was added to the second concentration liquid 20 with the amount of 157 grams, thus the solution with the amount of 397 grams was created (Step 104).

(73) Then, the solution with the amount of 397 grams, which had ethanol concentration of approximately 80% by adding this ethanol 5, was put into a so-called shaking container (for example, a concentration flask), and the shaking container was heavily shaken (Step 106).

(74) Here, the shaking period and the number of shaking times are not restricted. To shake manually, it is considered that the shaking container is shaken by at least about several tens times, for example, strongly shaken in the vertical direction.

(75) The following is assumed. Heavily shaking the shake container, for example, in the vertical direction promotes transportation of the antioxidant substance with a high antioxidative potency, namely, higher ORAC value to an ethanol solution (relative permittivity: 24) side, which has lower polarity than that of water (relative permittivity: 80). It is considered that transportation and separation of an inhibitor of the antioxidant substance with a high ORAC value to the water side is promoted.

(76) That is, in the shake container, the solution with the ethanol concentration of approximately 80% is clearly separated into an ethanol part 21 with low polarity and a water part 22 with high polarity in the vertical direction.

(77) As illustrated in Step 108 of FIG. 9, for example, the ethanol part 21 with low polarity was transported to the upper part of a separatory funnel 31 while the water part 22, which had higher polarity than that of ethanol, was transported to the lower part of the container. Thus, the ethanol part 21 and the water part 22 were separated.

(78) The solution separated to the upper layer had the smaller density and specific gravity compared to the solution at the lower layer. Therefore, the solution moved to the upper layer side and was separated.

(79) Here, a third supernatant 18 separated to the upper layer side became to have 250 grams while a lower layer separate liquid (precipitate) 33 separated at the lower layer side became to have 147 g.

(80) The polarity, density, and specific gravity of the organic solvent will be described. It is considered that there is no proportional relationship between the amount of the polarity, density, and the value of the specific gravity of an organic solvent. Generally, considering with an example of water as a solvent used for extraction, water is a solvent with comparatively high polarity (relative permittivity of 80 as described above: the value of the relative permittivity is regarded as an index whether the polarity is high or low). Meanwhile, an organic solvent that has basically lower polarity than that of water typified by ethanol (relative permittivity: 24) such as alcohol has a smaller density and a specific gravity than that of the water. Accordingly, the organic solvent is transported to the layer upper than that of the water and separated.

(81) That is, in extraction or other processes, a solvent with lower polarity than that of water, for example, ethanol has a smaller density and a specific gravity than those of the solvent at the lower layer (water). Accordingly, the organic solvent is transported to the layer upper than that of the water and is separated.

(82) Whether the polarity is high or low is indicated based on electrical bias in a molecule. The electrical bias of water, to be short, the relative permittivity is 80, which is a large value; therefore, the water is regarded as a solvent with high polarity. As described above, the value of the relative permittivity is regarded as an index of the polarity level.

(83) Here, the third supernatant 18 including the ethanol transferred to the upper layer and separated was concentrated and then formed into a paste. The paste-like third supernatant 18 had a water content rate of 35.2%. It is considered to be preferred that the water content rate be between approximately 40% and approximately 10%.

(84) The ORAC value of the concentrated paste-like third supernatant 18 with the water content rate of 35.2% per gram was measured at 377 mol TE/g: micromoles Trolox-equivalent/gram, which is an extremely high ORAC value.

(85) In the 377 mol TE/g: micromoles Trolox-equivalent/gram, the 370 mol TE/g: micromoles Trolox-equivalent/gram was an ORAC value indicating hydrophilic antioxidative potency while 7 mol TE/g: micromoles Trolox-equivalent/gram was an ORAC value indicating oleophilic antioxidative potency.

(86) In view of this, it can be inferred that the concentrated paste-like third supernatant 18 with the water content rate of 35.2% incorporates not only a hydrophilic antioxidant substance but also an oleophilic antioxidant substance or an amphiphilic antioxidant substance.

(87) As illustrated in FIG. 10, the obtained third supernatant 18 of 250 grams was separated into a fourth supernatant 19 and a precipitate 23 by centrifugation using a continuous centrifuge 24 illustrated in FIG. 11 or similar apparatus (Step 110 and Step 112).

(88) It is considered that this centrifugation operation makes it possible to promote further transporting the antioxidant substance with high antioxidative potency, namely, higher ORAC value, to the second supernatant 19 side. The inhibitor of the antioxidant substance with a high ORAC value can possibly be further transported to the precipitate 23 side, thus facilitating separation.

(89) Next, the fourth supernatant 19 separated and obtained as described above (Step 112) was concentrated by, for example, a rotary evaporator, a reduced-pressure concentration kneader, or similar apparatus (Step 114).

(90) Thus, the concentration liquid of the paste-like fourth supernatant 19 with the water content rate of approximately 34.6% was created. The water content rate at this time is preferred to be in a range of approximately 10% to approximately 40%.

(91) The ORAC value of the concentration liquid of the fourth supernatant 19 per gram was measured (Step 116). The ORAC value indicated 389 mol TE/g: micromoles Trolox-equivalent/gram, which is further extremely high ORAC value.

(92) In the 389 mol TE/g: micromoles Trolox-equivalent/gram, the 380 mol TE/g: micromoles Trolox-equivalent/gram was an ORAC value indicating hydrophilic antioxidative potency while 9 mol TE/g: micromoles Trolox-equivalent/gram was an ORAC value indicating oleophilic antioxidative potency.

(93) In view of this, it can be inferred that the paste-like fourth supernatant 19 with the water content rate of approximately 34.6% incorporates not only a hydrophilic antioxidant substance but also a large amount of oleophilic antioxidant substance or an amphiphilic antioxidant substance.

(94) The centrifugation operation using the centrifuge 24 illustrated in FIG. 11 will be described.

(95) It is constituted, for example, the third supernatant 18 can be continuously injected from an injection pipe 25 of the continuous centrifuge 24 illustrated in FIG. 11 to the continuous centrifuge 24.

(96) Here, the injection of the predetermined amount of the third supernatant 18 in the continuous centrifuge 24 is confirmed, and the continuous centrifuge 24 is operated. Thus, the third supernatant 18 is continuously separated into the so-called the precipitate 23 and the fourth supernatant 19.

(97) As seen from FIG. 11, the so-called precipitate 23 was collected to the outer periphery sidewall 13 side of the storage tank 12 by a centrifugal force. Apart from that, the so-called fourth supernatant 19 was delivered from upward of the storage tank 12 to the outside via the delivery pipe 14.

(98) In the present invention, it was confirmed that the fourth supernatant 19 incorporated not only a hydrophilic antioxidant substance with extremely high antioxidative potency and high ORAC value but also an oleophilic antioxidant substance or an amphiphilic antioxidant substance as described above.

(99) ORAC Company in the United States of America makes a database of ORAC values of various food products as already described. The graph of the ORAC values is illustrated in FIG. 12. As seen from FIG. 6, even a blueberry, which is recognized as having a high ORAC value by ORAC Company in the United States of America, the ORAC value is 66.2 mole TE/g.

(100) In contrast to this, it can be seen that the paste-like fourth supernatant 19 with the water content rate of approximately 34.6% in this working example incorporates an antioxidant substance with the ORAC value of 389 mole TE/g: micromoles Trolox-equivalent/gram, which is a value regarded as having high antioxidative potency and ORAC value approximately equal to or more than five times the ORAC value of the blueberry.

(101) Ethanol was added to the fourth supernatant 19 concentrated in Step 114 again (Step 118). The fourth supernatant 19 was repeatedly centrifuged with the continuous centrifuge 24 according to the present invention. The fourth supernatant 19 was allowed to be further separated. An antioxidant substance with further extremely high ORAC value can be collected, for example, in the fifth supernatant or the sixth supernatant concentrated to a paste shape after the separation.

LIST OF REFERENCE SYMBOLS

(102) 1 water 2 extraction container 3 oyster meat 4 concentration liquid 5 ethanol 6 precipitate 7 supernatant 8 continuous centrifuge 9 injection pipe 10 left side delivery pipe 11 right side delivery pipe 12 storage tank 13 outer periphery sidewall 14 delivery pipe 15 centrifugation precipitate 16 centrifugation supernatant 17 second supernatant 18 third supernatant 19 fourth supernatant 20 second concentration liquid 21 ethanol part 22 water part 24 continuous centrifuge 25 injection pipe 31 reparatory funnel 33 lower layer separate liquid