WO2010074164A1 - 水存在下における親油性成分の分解・劣化を抑制する方法 - Google Patents
水存在下における親油性成分の分解・劣化を抑制する方法 Download PDFInfo
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- WO2010074164A1 WO2010074164A1 PCT/JP2009/071473 JP2009071473W WO2010074164A1 WO 2010074164 A1 WO2010074164 A1 WO 2010074164A1 JP 2009071473 W JP2009071473 W JP 2009071473W WO 2010074164 A1 WO2010074164 A1 WO 2010074164A1
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- cyclodextrin
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Images
Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/73—Polysaccharides
- A61K8/738—Cyclodextrins
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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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
- A23L2/60—Sweeteners
-
- 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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
- A23L27/18—Mustard
-
- 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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/70—Fixation, conservation, or encapsulation of flavouring agents
- A23L27/75—Fixation, conservation, or encapsulation of flavouring agents the flavouring agents being bound to a host by chemical, electrical or like forces, e.g. use of precursors
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/33—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing oxygen
- A61K8/36—Carboxylic acids; Salts or anhydrides thereof
- A61K8/361—Carboxylic acids having more than seven carbon atoms in an unbroken chain; Salts or anhydrides thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/63—Steroids; Derivatives thereof
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/40—Chemical, physico-chemical or functional or structural properties of particular ingredients
- A61K2800/52—Stabilizers
Definitions
- the present invention relates to a method for suppressing decomposition / deterioration of lipophilic components.
- Lipophilic components are decomposed and deteriorated by interaction with water or by interaction with light, enzyme, oxygen, heat, etc. in the presence of water.
- an isothiocyanate clathrated with cyclodextrin is kneaded with a synthetic resin to be formed into a film, a sheet, a tray, or included in a printing ink or paint to form a film.
- a food packaging material that improves the stability of isothiocyanate by printing or coating and retains the antibacterial effect of isothiocyanate even after heat drying (Patent Document 1).
- JP 7-46973 A Japanese Patent Laid-Open No. 10-231224
- An object of the present invention is to provide a method for suppressing decomposition / degradation of lipophilic components by interaction with water or by interaction with light, enzyme, oxygen, heat, etc. in the presence of water.
- the present invention provides a method for suppressing degradation / degradation of a lipophilic component in the presence of water, and this method forms a complex comprising a lipophilic component, a plant sterol ester and a cyclodextrin, and the form of the complex And storing the new oil component in the presence of water.
- degradation / degradation of lipophilic components due to interaction with water or due to interaction with light, enzyme, oxygen, heat, etc. in the presence of water can be suppressed over time.
- the lipophilic component to which the present invention is applied is a lipophilic component that is decomposed and deteriorated by interaction with water or by interaction with light, enzyme, oxygen, heat, etc. in the presence of water.
- mustard extract containing allyl isothiocyanate e.g., mustard extract containing allyl isothiocyanate
- turmeric extracts such as curcumin, capsaicinoids, capsicum extract containing capsinoids, gingerol, gingerol, gingerol containing gingerone, piperine, etc.
- Preferable pepper extract docosahexaenoic acid (DHA), eicosapentaenoic acid (EPA), and other unsaturated fatty acids that are easily oxidized.
- DHA docosahexaenoic acid
- EPA eicosapentaenoic acid
- the mustard extract containing allyl isothiocyanate has the property of being easily degraded over time in the presence of water.
- a turmeric extract such as curcumin has a property of being easily decomposed over time by interaction with light in the presence of water.
- capsaicinoids have the property of being easily degraded over time by the interaction with enzymes in the presence of water.
- Capsinoids have a property that they are easily decomposed over time in the presence of water.
- ginger extracts such as gingerol, gingerol and gingerone have the property of being easily degraded over time in the presence of water.
- pepper extract such as piperine, has the property of being easily degraded over time in the presence of water.
- unsaturated fatty acids such as docosahexaenoic acid and eicosapentaenoic acid have the property of being decomposed and deteriorated over time by the interaction with oxygen in the presence of water.
- the plant sterol ester used in the present invention is a substance obtained by esterifying a fatty acid with a hydroxyl group in the sterol skeleton of a plant sterol.
- Examples of the method for producing a plant sterol ester include an enzyme method using an enzyme.
- Examples of the enzymatic method include a method in which a plant sterol ester is obtained by using lipase or the like as a catalyst, mixing plant sterol and a fatty acid, and reacting them (at 30 to 50 ° C. for about 48 hours).
- plant sterols include sterols contained in vegetable oils and fats, such as those extracted and purified from vegetable oils such as soybeans, rapeseed, and cottonseed, and ⁇ -sitosterol, campesterol, stigmasterol, It may be a mixture containing brush casterol, fucosterol, dimethyl sterol and the like.
- soy sterols include 53-56% sitosterol, 20-23% campesterol and 17-21% stigmasterol.
- What is marketed as "phytosterol F” (made by Tama Seikagaku Corporation) can also be used as plant sterol.
- the fatty acid may be derived from plants, such as those derived from rapeseed oil or palm oil, or may be derived from animals.
- Examples include myristic acid, stearic acid, palmitic acid, arachidonic acid, oleic acid, linoleic acid, ⁇ -linolenic acid, ⁇ -linolenic acid, eicosapentaenoic acid, docosahexaenoic acid, palmitooleic acid, lauric acid and the like.
- Preferred plant sterol esters include plant sterols obtained from soybean-derived plant sterols and fatty acids derived from rapeseed oil, and plant sterols obtained from soybean and rapeseed-derived plant sterols and palm oil-derived fatty acids.
- the former includes “Santosterol NO. 3” from Saneigen FFI Co., Ltd., and the latter includes “Plant Sterol Fatty Acid Esters” from Tama Biochemical Co., Ltd.
- the cyclodextrin used in the present invention is a cyclic non-reducing maltooligosaccharide having glucose as a structural unit.
- Cyclodextrin can be any of ⁇ -cyclodextrin, 6 ⁇ -cyclodextrin and 8 ⁇ -cyclodextrin with 6 glucose, but it is decomposed by human digestive enzymes and soluble in water ⁇ -cyclodextrin is preferred because it is high in food and drink, and particularly easy to use in beverages.
- the above-mentioned lipophilic component, a plant sterol ester and a cyclodextrin are formed into a complex, and the novel oily component is stored in the presence of water in the form of the complex, thereby interacting with water. Or degradation of lipophilic components over time due to interaction with light, enzymes, oxygen, heat, etc. in the presence of water.
- the complex here can be produced by a method including a complexing step in which a lipophilic component, a plant sterol ester, and a cyclodextrin are mixed to form a complex in the presence of water.
- the amount of the plant sterol ester is preferably 0.5 to 30000 parts by weight with respect to 1 part by weight of the lipophilic component, for example.
- the addition amount of the cyclodextrin mentioned later increases and the ratio of a lipophilic component becomes relatively low.
- the amount of cyclodextrin is, for example, preferably 0.01 to 1000 parts by weight, more preferably 0.1 to 100 parts by weight with respect to 1 part by weight of the plant sterol ester.
- the amount of water coexisting in the production of the complex is preferably 0.01 to 100 parts by weight, for example, 0.1 to 10 parts by weight with respect to 1 part by weight of cyclodextrin. More preferred.
- the mixing is preferably performed by heating at 40 to 90 ° C., more preferably 50 to 85 ° C.
- the order of addition and mixing of water, a new oil component, a plant sterol ester, and a cyclodextrin when producing the complex is not particularly limited.
- a mixture of a new oil component and a plant sterol ester (and water in the case of poor dispersibility) to prepare a mixture, while cyclodextron is dispersed in water to prepare another mixture, then both mixtures are preferably mixed.
- the mixing conditions and means are not limited as long as they are appropriately dispersed.
- a mixing device having a strong shearing force such as a kneader in order to sufficiently knead to form a complex.
- the new oil component is stored in the presence of water in the form of the composite thus obtained. More specifically, for example, in the form of a complex obtained in this way, by adding to and stored in foods and drinks, pharmaceuticals, cosmetics, etc. containing water, by interaction with water or in the presence of water The degradation and degradation of lipophilic components due to the interaction with light, enzymes, oxygen, heat, etc. can be suppressed over time.
- Example 1 To 5.67 parts by weight of the plant sterol ester dissolved by heating at 60 ° C., 0.63 parts by weight of mustard essential oil was added and dissolved. Meanwhile, 62.4 parts by weight of ⁇ -cyclodextrin and 31.3 parts by weight of water (75 ° C.) were added to the mortar and mixed with a pestle to obtain a paste. The plant sterol ester which melt
- Comparative Example 1 In a mortar, 66.24 parts by weight of ⁇ -cyclodextrin and 33.13 parts by weight of water (60 ° C.) were added and mixed with a pestle to obtain a paste. To this, 0.63 parts by weight of mustard essential oil was added and kneaded in a hot water bath (75 ° C.) for 10 minutes. After the kneading was completed, the scattered water was added and kneaded again uniformly. The amount (g) of Comparative Example 1 is shown in Table 1 below.
- Example 2 0.07 parts by weight of capsicum oleoresin was added to and dissolved in 3.5 parts by weight of the plant sterol ester heated and dissolved at 60 ° C. To the mortar, 64.3 parts by weight of ⁇ -cyclodextrin and 32.13 parts by weight of water (60 ° C.) were added and mixed with a pestle to obtain a paste. To this was added the plant sterol ester in which the aforementioned capsicum oleoresin was dissolved, and the mixture was kneaded in a hot water bath (60 ° C.) for 10 minutes. After the kneading was completed, the scattered water was added and kneaded again uniformly. The amount (g) of Example 2 is shown in Table 2 below.
- Comparative Example 2 66.6 parts by weight of ⁇ -cyclodextrin and 33.33 parts by weight of water (60 ° C.) were added to the mortar and mixed with a pestle to obtain a paste. To this, 0.07 part by weight of capsicum oleoresin was added and kneaded in a hot water bath (60 ° C.) for 10 minutes. After the kneading was completed, the scattered water was added and kneaded again uniformly. The amount (g) of Comparative Example 2 is shown in Table 2 below.
- Example 2 and Comparative Example 2 Each sample obtained in Example 2 and Comparative Example 2 was diluted 10-fold with 50 mM Tris buffer (capsaicin concentration 0.0028%). Acylase was added to this so that it might become 0.05 u / ml. The enzyme was reacted by shaking in a 37 ° C constant temperature water bath.
- a capsaicin reagent (capsaicin content of 95% or more) manufactured by SIGMA was diluted with 50 mM Tris buffer so that the capsaicin concentration was the same (0.0028%) as in Example 2 and Comparative Example 2.
- Acylase was added to a concentration of 05 u / ml. In the same manner as in Example 2 and Comparative Example 2, the mixture was shaken in a 37 ° C. constant temperature water bath to react with the enzyme.
- Fig. 2 shows changes in capsaicin concentration.
- the capsicum oleoresin is formed by forming a complex with a plant sterol ester and ⁇ -cyclodextrin and storing the capsicum oleoresin in the form of the complex in the presence of water.
- the degradation of capsaicin was clearly suppressed.
- the capsaicin remaining rate after the enzyme reaction for 60 minutes with respect to the start of shaking was 78.6% in Example 2, 58.9% in Comparative Example 2, and 2.0% in the Reference Example.
- capsinoids those extracted from “Natura” manufactured by Ajinomoto Co., Inc. were used. 0.35 parts by weight of fats and oils containing capsinoids was added to and dissolved in 0.70 parts by weight of the plant sterol ester heated to 70 ° C. On the other hand, 7.0 parts by weight of ⁇ -cyclodextrin and 3.5 parts by weight of water were placed in a mortar and mixed in a 70 ° C. hot water bath to obtain a paste. To this was added 1.05 parts by weight of the oil phase in which the capsinoids were dissolved, and the mixture was kneaded in a 70 ° C. hot water bath for 10 minutes to prepare a composite.
- the complex-containing model beverage was heated to a temperature of 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled in a pouch. Thereafter, it was kept in a constant temperature water bath at 83 ° C. for 7 minutes, and then sterilized.
- capsinoids those extracted from “Natura” manufactured by Ajinomoto Co., Inc. were used. 0.37 parts by weight of fats and oils containing capsinoids were added to and dissolved in 0.70 parts by weight of rapeseed white drawn oil heated to 70 ° C. Add 0.33 parts by weight of emulsifier (polyglycerin fatty acid ester SWA-10D manufactured by Mitsubishi Chemical Foods Co., Ltd.) and 1.05 parts by weight of the oil phase in which the capsinoids are dissolved to 10.2 parts by weight of water, and emulsify with a mixer. An emulsion was prepared.
- the obtained emulsion, 11.58 parts by weight, 0.56 parts by weight of citric acid and 0.27 parts by weight of trisodium citrate are dispersed in 87.6 parts by weight of water, and stirred for 30 seconds with a mixer.
- a beverage was prepared.
- the emulsion-containing model beverage was heated to a temperature of 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled into a pouch. Thereafter, it was kept in a constant temperature water bath at 83 ° C. for 7 minutes, and then sterilized.
- capsinoids those extracted from “Natura” manufactured by Ajinomoto Co., Inc. were used. 0.37 parts by weight of fats and oils containing capsinoids were added to and dissolved in 0.70 parts by weight of rapeseed white drawn oil heated to 70 ° C.
- 7.0 parts by weight of ⁇ -cyclodextrin and 3.5 parts by weight of water were placed in a mortar and mixed in a 70 ° C. hot water bath to obtain a paste.
- the complex-containing model beverage was heated to a temperature of 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled in a pouch. Thereafter, it was kept in a constant temperature water bath at 83 ° C. for 7 minutes, and then sterilized.
- Example 3 The model beverages prepared in Example 3 and Comparative Examples 3-1 and 3-2 were stored at 40 ° C. Samples of capsinoids after a certain period of time were quantified by liquid chromatography. The residual ratio of capsinoids was expressed as a percentage of the value of capsinoids immediately after the start of storage (day 0) as 100%, and the values after 1 day, 5 days, and 25 days after storage at 40 ° C. The results are shown in FIG. As is clear from FIG. 3, Example 3 can significantly suppress the degradation of capsinoids when stored at 40 ° C., as compared with Comparative Examples 3-1 and 3-2. From the above results, it was found that the present invention can suppress the decomposition of capsinoids in the presence of water and can improve the stability.
- Example 3 and Comparative Example 3-2 Liquid Chromatography Pretreatment Method
- 12.5 g of model beverage was centrifuged (3000 rpm for 10 minutes), the supernatant was removed, 6 ml of DMSO (dimethyl sulfoxide) was added, and Sonic was applied to dissolve the precipitate. Further, the volume was made up to 25 ml with methanol, and after filtration through a 0.45 ⁇ m filter, a test solution was obtained.
- Comparative Example 3-1 5 g of a model beverage was collected, made up to a volume of 10 ml with methanol, filtered through a 0.45 ⁇ m filter, and used as a test solution.
- Example 4 As the ginger extract, a supercritical ginger extract (gingerol: 24.8% gingerol: 10.7% Takasago fragrance) was used. To 0.18 parts by weight of plant sterol ester heated to 80 ° C. and 0.12 parts by weight of edible fats and oils, 0.015 parts by weight of ginger extract was added and dissolved. On the other hand, 1.093 parts by weight of ⁇ -cyclodextrin and 1.093 parts by weight of water were mixed with a TK homomixer while heating to 80 ° C.
- the ginger extract complex-containing model beverage was heated to 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled into a pouch. Then, it kept at 83 degreeC for 5 minute (s) in the constant temperature water tank, and performed post-sterilization.
- the produced ginger extract complex-containing model beverage had a gingerol component of 36.1 ppm and a gingerol component of 15.4 ppm.
- emulsified preparation obtained by emulsifying the ginger extract (gingerol: 1.79% gingerol 0.89% Takasago flavor) was used.
- Emulsified preparation 0.23 parts by weight, citric acid 0.3 part by weight, trisodium citrate 0.12 part by weight is dispersed in 99.35 parts by weight of water, and stirred for 30 seconds with a mixer.
- a beverage was prepared.
- the ginger extract emulsion preparation model beverage was heated to a temperature of 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled in a pouch. Then, it kept at 83 degreeC for 5 minute (s) in the constant temperature water tank, and performed post-sterilization.
- the gingerol component of the produced ginger extract emulsified preparation-containing model beverage was 40.9 ppm, and the gingerol component was 16.2 ppm.
- Example 4 The model beverage prepared in Example 4 and Comparative Example 4 was stored at 60 ° C. Samples of gingerol and gingerol were quantified by liquid chromatography before storage, one week and two weeks later. As for the remaining ratio of gingerol and gingerol, each value before storage (week 0) was taken as 100%, and the value after 1 week after storage and the value after 2 weeks were expressed as percentages. The results are shown in FIGS. As is clear from FIGS. 4 and 5, Example 4 suppresses the decomposition of gingerol, particularly gingerol, as compared with Comparative Example 4. From the above results, it was found that the present invention can suppress the decomposition of ginger extract in the presence of water and can improve the stability.
- Example 4 Liquid Chromatography Pretreatment Method
- 25 g of model beverage was centrifuged (3000 rpm for 10 minutes), the supernatant was removed, 3 ml of DMSO (dimethyl sulfoxide) was added, and the precipitate was dissolved by applying ultrasonic waves. did. Furthermore, the solution was made up to 50 ml with methanol, filtered through a 0.45 ⁇ m filter, and used as a test solution.
- DMSO dimethyl sulfoxide
- Example 5 As the pepper extract, piperine powder (piperin content: 92% or more, rice field flavor) was used. To 0.18 parts by weight of plant sterol ester heated to 80 ° C. and 0.12 parts by weight of edible fats and oils, 0.0064 parts by weight of pepper extract was added and dissolved. On the other hand, 1.097 parts by weight of ⁇ -cyclodextrin and 1.097 parts by weight of water were mixed with a TK homomixer while heating to 80 ° C. To this was added 0.3064 parts by weight of the oil phase in which the pepper extract was dissolved, and the mixture was then stirred with a TK homomixer while warming at 80 ° C. to perform preliminary emulsification.
- piperine powder piperin content: 92% or more, rice field flavor
- a high-pressure homogenizer (lab 1000, LAB1000 pressure: 100 MPa) was passed to prepare a pepper extract-containing composite. 2.5 parts by weight of the resulting composite, 0.3 part by weight of citric acid and 0.12 part by weight of trisodium citrate are dispersed in 97.08 parts by weight of water, and stirred for 30 seconds with a mixer.
- a body-containing model beverage was prepared.
- the pepper extract complex-containing model beverage was heated to 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled into a pouch. Then, it kept at 83 degreeC for 5 minute (s) in the constant temperature water tank, and performed post-sterilization.
- the amount of piperine contained in the prepared pepper extract complex-containing model beverage was 62 ppm.
- pepper extract (piperine content: 300-1400 ppm Maruzen Pharmaceutical) was used. Disperse 0.15 parts by weight of pepper extract, 0.3 part by weight of citric acid and 0.12 part by weight of trisodium citrate in 99.43 parts by weight of water, and stir with a mixer for 30 seconds. Was made.
- the pepper extract-containing model beverage was heated to 93 ° C., sterilized by holding at 90 ° C. for 3 minutes, and then filled into a pouch. Then, it kept at 83 degreeC for 5 minute (s) in the constant temperature water tank, and performed post-sterilization. The amount of piperine contained in the prepared pepper extract-containing model beverage was 0.25 ppm.
- Example 5 The model beverage prepared in Example 5 and Comparative Example 5 was stored at 60 ° C. Samples of piperine before storage, one week and two weeks later were quantified by liquid chromatography. The residual ratio of piperine was expressed as a percentage after 1 week of storage and 2 weeks after storage of piperine before storage (week 0) as 100%. The results are shown in FIG. As is clear from FIG. 6, Example 5 suppressed the decomposition of piperine as compared with Comparative Example 5. From the above results, it was found that the present invention can suppress the decomposition of the pepper extract in the presence of water and can improve the stability.
- Example 5 Liquid Chromatography Pretreatment Method For Example 5, 10 g of model drink was centrifuged (3000 rpm for 10 minutes), the supernatant was removed, 3 ml of DMSO (dimethyl sulfoxide) was added, and the precipitate was dissolved by applying ultrasonic waves. did. Furthermore, the solution was made up to 50 ml with methanol, filtered through a 0.45 ⁇ m filter, and used as a test solution. For Comparative Example 5, after dilution with methanol, the solution was filtered through a 0.45 ⁇ m filter.
- DMSO dimethyl sulfoxide
- odorless processed fish oil “DHA-22HG” manufactured by Maruha Nichiro Foods Co., Ltd.
- odorless processed fish oil “DHA-22HG” manufactured by Maruha Nichiro Foods Co., Ltd.
- 10 parts by weight of ⁇ -cyclodextrin and 5 parts by weight of water (90 ° C.) were mixed to prepare a mixture (paste).
- a plant sterol ester in which odorless processed DHA-containing fish oil was dissolved was added to the mixed paste, and the mixture was kneaded for 10 minutes while heating to 70 ° C. using a mortar to prepare a composite.
- 82.895 parts by weight of water was added and mixed, and then 0.5 parts by weight of citric acid and 0.25 parts by weight of trisodium citrate were added and mixed.
- the white liquid was stirred and the temperature reached 93 ° C., it was filled in a colorless and transparent glass container, and then cooled to produce a beverage containing the container.
- pH of this drink was 3.4.
- a plant sterol ester in which odorless processed DHA-containing fish oil was dissolved was added to the emulsion, and the mixture was stirred with a homomixer at 5000 rpm for 10 minutes to prepare an emulsion.
- 82.895 parts by weight of water was added and mixed, and then 0.5 parts by weight of citric acid and 0.25 parts by weight of trisodium citrate were added and mixed. Thereafter, after reaching a temperature of 93 ° C. with stirring, it was filled in a colorless and transparent glass container and then cooled to produce a container-containing beverage.
- pH of this drink was 3.4.
- rapeseed white squeezed oil in which odorless processed DHA-containing fish oil was dissolved was added and stirred with a homomixer at 5000 rpm for 10 minutes to prepare an emulsion.
- 82.895 parts by weight of water was added and mixed, and then 0.5 parts by weight of citric acid and 0.25 parts by weight of trisodium citrate were added and mixed. Thereafter, after reaching a temperature of 93 ° C. with stirring, it was filled in a colorless and transparent glass container and then cooled to produce a container-containing beverage.
- pH of this drink was 3.4.
- Example 7 As an unsaturated fatty acid, odorless processed fish oil “DHA-22HG” (manufactured by Maruha Nichiro Foods Co., Ltd.) containing 22% or more of DHA was used. Add 0.455 parts by weight of odorless processed DHA-containing fish oil to 0.9 parts by weight of plant sterol ester, and stir this to warm and dissolve at 70 ° C to dissolve the odorless processed DHA-containing fish oil. Prepared. Separately, 10 parts by weight of ⁇ -cyclodextrin and 5 parts by weight of water (90 ° C.) were mixed to prepare a mixture (paste).
- a plant sterol ester in which odorless processed DHA-containing fish oil was dissolved was added to the mixed paste, and the mixture was kneaded for 10 minutes while heating to 70 ° C. using a mortar to prepare a composite.
- 82.895 parts by weight of water was added and mixed, and then 0.5 parts by weight of citric acid and 0.25 parts by weight of trisodium citrate were added and mixed.
- the white liquid was stirred and the temperature reached 93 ° C., it was filled in a colorless and transparent glass container, and then cooled to produce a beverage containing the container.
- pH of this drink was 3.4.
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Abstract
Description
一方、シクロデキストリンを溶解した水、又は親水性溶液に脂溶性L-アスコルビン酸高級脂肪酸エステルを加え、50~100℃でかき混ぜる事によって、経時的安定性、及び熱安定性を持ったL-アスコルビン酸高級脂肪酸エステル類の親水性複合体を得ることが出来る(特許文献2)。しかしながら、この方法では包接時に水、又は親水性溶媒と接触する上、高温にさらされる為、特に水存在下で不安定な物質に関しては分解等の反応が起こり易いという課題があった。又、得られた複合体の安定性も充分とは言えなかった。
植物性ステロールとしては、植物油脂中に含まれるステロールなどが挙げられ、例えば大豆、菜種、綿実などの植物油脂から抽出・精製されたものであり、β-シトステロール、カンペステロール、スチグマステロール、ブラシカステロール、フコステロール、ジメチルステロールなどを含む混合物であってもよい。例えば、大豆ステロールには、53~56%のシトステロール、20~23%のカンペステロール及び17~21%のスチグマステロールが含まれる。植物性ステロールとして、「フィトステロール F」(タマ生化学工業株式会社製)として市販されているものを使用することもできる。
脂肪酸としては、植物由来のもの、例えば菜種油、パーム油由来のものであってもよく、又は動物由来のものであってもよい。例えば、ミリスチン酸、ステアリン酸、パルミチン酸、アラキドン酸、オレイン酸、リノール酸、α-リノレン酸、γ-リノレン酸、エイコサペンタエン酸、ドコサヘキサエン酸、パルミトオレイン酸、ラウリン酸などが挙げられる。
好ましい植物ステロールエステルとしては、大豆由来の植物ステロールと菜種油由来の脂肪酸から得られる植物ステロールや大豆及び菜種由来の植物ステロールとパーム油由来の脂肪酸から得られる植物ステロールなどが挙げられる。前者には、三栄源エフ・エフ・アイ(株)の「サンステロールNO.3」などがあり、後者には、タマ生化学(株)の「植物ステロール脂肪酸エステル」などがある。
シクロデキストリンを添加した後は、十分に混練して複合体を形成するために、ニーダ等のせん断力の強い混合装置を使用するのがよい。
本発明においては、このようにして得られた複合体の形態として前記新油性成分を水存在下で保存する。より具体的には、例えば、このようにして得られた複合体の形態として水を含む飲食品、医薬品、化粧品などに添加して保存することによって、水との相互作用による、又は水存在下における光、酵素、酸素、熱などとの相互作用による親油性成分の分解、劣化を経時的に抑制することができる。
60℃に加温溶解した植物ステロールエステル5.67重量部に対し、マスタードエッセンシャルオイル0.63重量部を添加して溶解した。一方で乳鉢にγシクロデキストリン62.4重量部及び水31.3重量部(75℃)を加えて乳棒で混合し、ペースト状とした。これに、前述のマスタードエッセンシャルオイルを溶解した植物ステロールエステルを加え、湯煎(75℃)中で10分間混練した。混練終了後、飛散した分の水を添加し、再度均一に混練した。実施例1の配合量(g)を下記表1に示す。
乳鉢にγシクロデキストリン66.24重量部及び水33.13重量部(60℃)を加えて乳棒で混合し、ペースト状とした。これに、マスタードエッセンシャルオイル0.63重量部を加え、湯煎(75℃)中で10分間混練した。混練終了後、飛散した分の水を添加し、再度均一に混練した。比較例1の配合量(g)を下記表1に示す。
実施例1及び比較例1で得られた各サンプル1重量部に対し、水5重量部を添加し、均一に分散させた。この水分散させた複合体サンプルをGC用バイアル瓶に満中充填し、キャップで密閉した後、アルミパウチに入れてシールした。これを50℃で保存した。
0日(保存開始時)、1日及び6日保存したサンプルをヘキサンで100倍に希釈し、16~18時間室温で放置し、0.45μmフィルターを通してGC検体とした。GC測定はFID検出器を使用し、以下の条件で測定した。
カラム:DB-WAX(内径0.53mm、長さ30m、膜厚1μm)
キャリアガス:ヘリウムガス
背圧:20kpa
注入口温度:200℃
検出器温度:220℃
昇温条件:100℃から180℃まで昇温(昇温速度 20℃/分)
アリル濃度の変化を図1に示す。図1に示されるように、植物ステロールエステル及びγシクロデキストリンと複合体を形成し、該複合体の形態にしてマスタードエッセンシャルオイルを水存在下で保存することにより、該オイル中のアリルイソチオシアネートの分解は明らかに抑制された。尚、保存開始時に対して、6日保存後のアリルイソチオシアネート残存率は、実施例1で60.2%、比較例1で15.5%であった。
60℃に加温溶解した植物ステロールエステル3.5重量部に対し、カプシカムオレオレジン0.07重量部を添加して溶解した。乳鉢にγシクロデキストリン64.3重量部及び水32.13重量部(60℃)を加えて乳棒で混合し、ペースト状とした。これに、前述のカプシカムオレオレジンを溶解した植物ステロールエステルを加え、湯煎(60℃)中で10分間混練した。混練終了後、飛散した分の水を添加し、再度均一に混練した。実施例2の配合量(g)を下記表2に示す。
乳鉢にγシクロデキストリン66.6重量部及び水33.33重量部(60℃)を加えて乳棒で混合し、ペースト状とした。これに、カプシカムオレオレジン0.07重量部を加え、湯煎(60℃)中で10分間混練した。混練終了後、飛散した分の水を添加し、再度均一に混練した。比較例2の配合量(g)を下記表2に示す。
実施例2及び比較例2で得られた各サンプルを50mMトリス緩衝液で10倍に希釈した(カプサイシン濃度 0.0028%)。これに0.05u/mlとなるようにアシラーゼを添加した。37℃恒温水槽中で振とうし、酵素を反応させた。
また、参考例として、SIGMA社製カプサイシン試薬(カプサイシン含量95%以上)を実施例2、比較例2とカプサイシン濃度が同じ(0.0028%)になるよう50mMトリス緩衝液で希釈し、これに0.05u/mlとなるようにアシラーゼを添加した。実施例2、比較例2と同様に37℃恒温水槽中で振とうし、酵素を反応させた。
0(振とう開始時)分、30分及び60分酵素を反応させたサンプル2mlに対し、水3mlを添加し、5mlに調整した。更に2.5N NaOHを1ml添加し、100℃沸騰水中で10分間加熱した。加熱後、メタノールを20ml添加した。2.5N HCl1mlを加え、メタノールで50mlに定容した後、0.45μmフィルターを通してHPLC検体とした。HPLC測定は、蛍光検出器を使用し、以下の条件で実施した。
カラム:ODS(センシュー科学)
流速:1ml/min
移動相:アセトニトリル:TFA=1:1
注入量:2μl
検出:ex270、em330
カプシノイド類として、味の素社製の「ナチュラ」より抽出したものを使用した。
70℃に加温した植物ステロールエステル0.70重量部に対し、カプシノイド類を含む油脂0.35重量部を添加して溶解した。一方で乳鉢に、γシクロデキストリン7.0重量部及び水3.5重量部を入れて、70℃湯浴で混合し、ペースト状とした。これに、上記のカプシノイド類を溶解した油相1.05重量部を加え、70℃湯浴中で10分間混練し、複合体を作製した。得られた複合体11.55重量部、クエン酸0.56重量部、クエン酸三ナトリウム0.27重量部を水87.6重量部に分散させ、ミキサーで30秒攪拌し、複合体含有モデル飲料を作製した。複合体含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃7分間保持し、後殺菌を行った。
カプシノイド類として、味の素社製の「ナチュラ」より抽出したものを使用した。
70℃に加温した菜種白絞油0.70重量部に対して、カプシノイド類を含む油脂0.35重量部を添加して溶解した。水10.2重量部に乳化剤0.33重量部(三菱化学フーズ社製 ポリグリセリン脂肪酸エステル SWA-10D)、上記のカプシノイド類を溶解した油相1.05重量部を加え、ミキサーで乳化させ、乳化物を作製した。得られた乳化物11.58重量部、クエン酸0.56重量部、クエン酸三ナトリウム0.27重量部を水87.6重量部に分散させ、ミキサーで30秒攪拌し、乳化物含有モデル飲料を作製した。乳化物含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃7分間保持し、後殺菌を行った。
カプシノイド類として、味の素社製の「ナチュラ」より抽出したものを使用した。
70℃に加温した菜種白絞油0.70重量部に対して、カプシノイド類を含む油脂0.35重量部を添加して溶解した。一方で乳鉢に、γシクロデキストリン7.0重量部及び水3.5重量部を入れて、70℃湯浴で混合し、ペースト状とした。これに、上記のカプシノイド類を溶解した油相1.05重量部を加え、70℃湯浴中で10分間混練し、複合体を作製した。得られた複合体11.55重量部、クエン酸0.56重量部、クエン酸三ナトリウム0.27重量部を水87.6重量部に分散させ、ミキサーで30秒攪拌し、複合体含有モデル飲料を作製した。複合体含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃7分間保持し、後殺菌を行った。
実施例3及び比較例3-2については、モデル飲料12.5gを遠心分離(3000rpm 10分間)後、上清を除去し、DMSO(ジメチルスルホキシド)6mlを添加し、超音波を当てて沈殿物を溶解した。さらに、メタノールで25mlに定容し、0.45μmフィルター濾過後、検液とした。
比較例3-1については、モデル飲料5gを採取し、メタノールで10mlに定容し、0.45μmフィルター濾過後、検液とした。
蛍光検出器使用
カラム mightysil (250mm φ2.0)
流速 0.2ml/min
注入量 3μl
移動相 pH3.3TFA水:アセトニトリル=20:80
検出FLD EX270 EM330
ショウガ抽出物として、超臨界ショウガ抽出物(ジンゲロール:24.8% ショウガオール:10.7% 高砂香料)を使用した。
80℃に加温した植物ステロールエステル0.18重量部、食用油脂0.12重量部に対し、ショウガ抽出物0.015重量部を添加して溶解した。一方で、γシクロデキストリン1.093重量部、水1.093重量部を80℃に加温しながらTKホモミキサーで混合した。これに、上記のショウガ抽出物を溶解した油相0.315重量部を加え、引き続き、80℃で加温しながらTKホモミキサーで攪拌し、予備乳化を行った。予備乳化後、高圧ホモジナイザー(エスエムティー社製 LAB1000 圧力:100MPa)を通過させ、ショウガ抽出物含有複合体を作製した。得られた複合体2.5重量部、クエン酸0.3重量部、クエン酸三ナトリウム0.12重量部を水97.08重量部に分散させ、ミキサーで30秒攪拌し、ショウガ抽出物複合体含有モデル飲料を作製した。ショウガ抽出物複合体含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃5分間保持し、後殺菌を行った。作製したショウガ抽出物複合体含有モデル飲料のジンゲロール成分は36.1ppmであり、ショウガオール成分は15.4ppmであった。
ここでは、ショウガ抽出物を乳化加工した乳化製剤(ジンゲロール:1.79% ショウガオール0.89% 高砂香料)を使用した。
乳化製剤0.23重量部、クエン酸0.3重量部、クエン酸三ナトリウム0.12重量部を水99.35重量部に分散させ、ミキサーで30秒攪拌し、ショウガ抽出物乳化製剤含有モデル飲料を作製した。ショウガ抽出物乳化製剤モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃5分間保持し、後殺菌を行った。作製したショウガ抽出物乳化製剤含有モデル飲料のジンゲロール成分は40.9ppmであり、ショウガオール成分は16.2ppmであった。
実施例4については、モデル飲料25gを遠心分離(3000rpm 10分間)後、上清を除去し、DMSO(ジメチルスルホキシド)3mlを添加し、超音波を当てて沈殿物を溶解した。さらに、メタノールで50mlに定容し、0.45μmフィルター濾過後、検液とした。
比較例4については、モデル飲料25gを採取し、メタノールで50mlに定容し、0.45μmフィルター濾過後、検液とした。
UV 282nm
カラム ODS C18 (センシュー科学)
流速 1.0ml/min
注入量 20μl
分析時間 30分
移動相 アセトニトリル:水:THF(テトラヒドロフラン)=45:50:5
コショウ抽出物として、ピペリン粉末(ピペリン含量:92%以上 稲畑香料)を使用した。
80℃に加温した植物ステロールエステル0.18重量部、食用油脂0.12重量部に対し、コショウ抽出物0.0064重量部を添加して溶解した。一方で、γシクロデキストリン1.097重量部、水1.097重量部を80℃に加温しながらTKホモミキサーで混合した。これに、上記のコショウ抽出物を溶解した油相0.3064重量部を加え、引き続き、80℃で加温しながらTKホモミキサーで攪拌し、予備乳化を行った。予備乳化後、高圧ホモジナイザー(エスエムティー社製 LAB1000 圧力:100MPa)を通過させ、コショウ抽出物含有複合体を作製した。得られた複合体2.5重量部、クエン酸0.3重量部、クエン酸三ナトリウム0.12重量部を水97.08重量部に分散させ、ミキサーで30秒攪拌し、コショウ抽出物複合体含有モデル飲料を作製した。コショウ抽出物複合体含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃5分間保持し、後殺菌を行った。作製したコショウ抽出物複合体含有モデル飲料に含まれるピペリン量は62ppmであった。
ここでは、コショウ科ヒハツ抽出物(ピペリン類含量:300~1400ppm 丸善製薬)を使用した。
コショウ抽出物0.15重量部、クエン酸0.3重量部、クエン酸三ナトリウム0.12重量部を水99.43重量部に分散させ、ミキサーで30秒攪拌し、コショウ抽出物含有モデル飲料を作製した。コショウ抽出物含有モデル飲料を93℃達温まで加熱し、3分間90℃保持で殺菌後、パウチに充填した。その後、恒温水槽中に83℃5分間保持し、後殺菌を行った。作製したコショウ抽出物含有モデル飲料に含まれるピペリン量は0.25ppmであった。
実施例5については、モデル飲料10gを遠心分離(3000rpm 10分間)後、上清を除去し、DMSO(ジメチルスルホキシド)3mlを添加し、超音波を当てて沈殿物を溶解した。さらに、メタノールで50mlに定容し、0.45μmフィルター濾過後、検液とした。
比較例5については、メタノールで希釈後、0.45μmフィルター濾過し、検液とした。
UV 343nm
カラム YMCPack ODS-A
流速 1.0ml/min
注入量 5μl
移動相 アセトニトリル:水:THF(テトラヒドロフラン)=45:55:7
不飽和脂肪酸として、DHAを22%以上含有する無臭加工魚油「DHA-22HG」((株)マルハニチロ食品社製)を使用した。
無臭加工DHA含有魚油0.455重量部を植物ステロールエステル0.9重量部に加え、これを攪拌しながら、70℃に加温溶解して、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを調製した。別途、γシクロデキストリン10重量部と水(90℃)5重量部とを混合して混合物(ペースト)を調製した。前記混合ペーストに、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを加え、乳鉢を用いて、70℃に加温しつつ10分間混練して複合体を調製した。上記複合体に、水82.895重量部を加えながら混合し、次いでクエン酸0.5重量部、クエン酸三ナトリウム0.25重量部を添加混合した。さらに、ホモミキサーで5000rpmで2分間攪拌し、均一な白色液を得た。白色液を攪拌しながら93℃達温後、無色透明のガラス容器に充填の後、冷却して容器入り飲料を製造した。尚、この飲料のpHは、3.4であった。
不飽和脂肪酸として、DHAを22%以上含有する無臭加工魚油「DHA-22HG」((株)マルハニチロ食品社製)を使用した。
無臭加工DHA含有魚油0.455重量部を植物ステロールエステル0.9重量部に加え、これを攪拌しながら、70℃に加温溶解して、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを調製した。別途、乳化剤0.5重量部を水(70℃)14.5重量部に溶解した。前記乳化液に、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを加え、ホモミキサーで5000rpmで10分間攪拌し、乳化液を調製した。上記乳化液に、水82.895重量部を加えながら混合し、次いでクエン酸0.5重量部、クエン酸三ナトリウム0.25重量部を添加混合した。その後、攪拌しながら93℃達温後、無色透明のガラス容器に充填の後、冷却して容器入り飲料を製造した。尚、この飲料のpHは、3.4であった。
不飽和脂肪酸として、DHAを22%以上含有する無臭加工魚油「DHA-22HG」((株)マルハニチロ食品社製)を使用した。
無臭加工DHA含有魚油0.455重量部を菜種白絞油0.9重量部に加え、これを攪拌しながら、70℃に加温溶解して、無臭加工DHA含有魚油を溶解させた菜種白絞油を調製した。別途、乳化剤0.5重量部を水(70℃)14.5重量部に溶解した。前記乳化液に、無臭加工DHA含有魚油を溶解させた菜種白絞油を加え、ホモミキサーで5000rpmで10分間攪拌し、乳化液を調製した。上記乳化液に、水82.895重量部を加えながら混合し、次いでクエン酸0.5重量部、クエン酸三ナトリウム0.25重量部を添加混合した。その後、攪拌しながら93℃達温後、無色透明のガラス容器に充填の後、冷却して容器入り飲料を製造した。尚、この飲料のpHは、3.4であった。
容器入り飲料を、恒温槽(「SANYO GROWTH CABINET」、温度25℃、照度1万ルクス)に入れ、6日間保存した。保存後の飲料の臭い(魚臭)を官能評価した。配合及び官能評価の結果を下記表6に示す。この結果より、本発明によって、無臭加工DHA含有魚油の劣化を抑制できることが分かった。
不飽和脂肪酸として、DHAを22%以上含有する無臭加工魚油「DHA-22HG」((株)マルハニチロ食品社製)を使用した。
無臭加工DHA含有魚油0.455重量部を植物ステロールエステル0.9重量部に加え、これを攪拌しながら、70℃に加温溶解して、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを調製した。別途、γシクロデキストリン10重量部と水(90℃)5重量部とを混合して混合物(ペースト)を調製した。前記混合ペーストに、無臭加工DHA含有魚油を溶解させた植物ステロールエステルを加え、乳鉢を用いて、70℃に加温しつつ10分間混練して複合体を調製した。上記複合体に、水82.895重量部を加えながら混合し、次いでクエン酸0.5重量部、クエン酸三ナトリウム0.25重量部を添加混合した。さらに、ホモミキサーで5000rpmで2分間攪拌し、均一な白色液を得た。白色液を攪拌しながら93℃達温後、無色透明のガラス容器に充填の後、冷却して容器入り飲料を製造した。尚、この飲料のpHは、3.4であった。
不飽和脂肪酸として、DHAを22%以上含有する無臭加工魚油「DHA-22HG」((株)マルハニチロ食品社製)を使用した。
γシクロデキストリン10重量部と水(90℃)5重量部とを混合して混合物(ペースト)を調製した。前記混合ペーストに、無臭加工DHA含有魚油を加え、乳鉢を用いて、70℃に加温しつつ10分間混練して複合体を調製した。上記複合体に、水83.795重量部を加えながら混合し、次いでクエン酸0.5重量部、クエン酸三ナトリウム0.25重量部を添加混合した。さらに、ホモミキサーで5000rpmで2分間攪拌し、均一な白色液を得た。白色液を攪拌しながら93℃達温後、無色透明のガラス容器に充填の後、冷却して容器入り飲料を製造した。尚、この飲料のpHは、3.4であった。
容器入り飲料を、恒温槽(「SANYO GROWTH CABINET」、温度25℃、照度1万ルクス)に入れ、6日間保存した。保存後の飲料の臭い(魚臭)を官能評価した。さらに、過酸化物価(試験方法:酢酸-イソオクタン法)を測定した。配合及び官能評価の結果を下記表7に示す。この結果より、本発明によって、無臭加工DHA含有魚油の劣化を抑制できることが分かった。
Claims (2)
- 水存在下における親油性成分の分解・劣化を抑制する方法であって、
親油性成分、植物ステロールエステル及びシクロデキストリンを含む複合体を形成し、該複合体の形態にして前記新油性成分を水存在下で保存することを特徴とする前記方法。 - 前記親油性成分がカラシ抽出物、トウガラシ抽出物、ショウガ抽出物、コショウ抽出物、不飽和脂肪酸及びウコン抽出物からなる群より選ばれる、請求項1記載の方法。
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JP2010544128A JP5543372B2 (ja) | 2008-12-24 | 2009-12-24 | 水存在下における親油性成分の分解・劣化を抑制する方法 |
CN2009801548311A CN102281773A (zh) | 2008-12-24 | 2009-12-24 | 抑制亲油性成分在水的存在下分解·劣化的方法 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2012050346A (ja) * | 2010-08-31 | 2012-03-15 | House Foods Corp | 容器詰ショウガ飲料 |
JP2012085615A (ja) * | 2010-10-22 | 2012-05-10 | House Foods Corp | 複合体を含有する組成物及びその製造方法 |
JP2013531052A (ja) * | 2010-07-23 | 2013-08-01 | アウリガ インターナショナル | スルフォラファンの安定化 |
WO2013157118A1 (ja) * | 2012-04-19 | 2013-10-24 | ハウス食品株式会社 | 複合体を含有する組成物及びその製造方法 |
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- 2009-12-24 KR KR1020117016953A patent/KR20110110206A/ko not_active Application Discontinuation
- 2009-12-24 US US13/141,285 patent/US20110256283A1/en not_active Abandoned
- 2009-12-24 CN CN2009801548311A patent/CN102281773A/zh active Pending
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JP2012085615A (ja) * | 2010-10-22 | 2012-05-10 | House Foods Corp | 複合体を含有する組成物及びその製造方法 |
WO2013157118A1 (ja) * | 2012-04-19 | 2013-10-24 | ハウス食品株式会社 | 複合体を含有する組成物及びその製造方法 |
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