WO2004110163A1 - 加工された大豆βーコングリシニンたん白 - Google Patents
加工された大豆βーコングリシニンたん白 Download PDFInfo
- Publication number
- WO2004110163A1 WO2004110163A1 PCT/JP2003/009282 JP0309282W WO2004110163A1 WO 2004110163 A1 WO2004110163 A1 WO 2004110163A1 JP 0309282 W JP0309282 W JP 0309282W WO 2004110163 A1 WO2004110163 A1 WO 2004110163A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- protein
- conglycinin
- heating
- conglycinin protein
- powder
- Prior art date
Links
- 108700037728 Glycine max beta-conglycinin Proteins 0.000 title abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 235000013305 food Nutrition 0.000 claims abstract description 34
- 230000002378 acidificating effect Effects 0.000 claims abstract description 18
- 108090000623 proteins and genes Proteins 0.000 claims description 93
- 102000004169 proteins and genes Human genes 0.000 claims description 93
- 238000000034 method Methods 0.000 claims description 30
- 230000007935 neutral effect Effects 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 4
- 230000036571 hydration Effects 0.000 abstract description 13
- 238000006703 hydration reaction Methods 0.000 abstract description 13
- 238000012545 processing Methods 0.000 abstract description 7
- 235000018102 proteins Nutrition 0.000 description 89
- 239000000843 powder Substances 0.000 description 33
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 24
- 239000000243 solution Substances 0.000 description 21
- 239000000203 mixture Substances 0.000 description 15
- 244000068988 Glycine max Species 0.000 description 10
- 235000010469 Glycine max Nutrition 0.000 description 10
- 235000011121 sodium hydroxide Nutrition 0.000 description 9
- 238000004090 dissolution Methods 0.000 description 8
- 240000007594 Oryza sativa Species 0.000 description 7
- 235000007164 Oryza sativa Nutrition 0.000 description 7
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- 239000000796 flavoring agent Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 7
- 235000009566 rice Nutrition 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 108010073771 Soybean Proteins Proteins 0.000 description 6
- 235000013361 beverage Nutrition 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
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- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
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- 230000003179 granulation Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 235000013536 miso Nutrition 0.000 description 3
- 235000002949 phytic acid Nutrition 0.000 description 3
- 229940001941 soy protein Drugs 0.000 description 3
- 235000019710 soybean protein Nutrition 0.000 description 3
- 238000001694 spray drying Methods 0.000 description 3
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- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 235000005979 Citrus limon Nutrition 0.000 description 2
- 244000131522 Citrus pyriformis Species 0.000 description 2
- 239000004278 EU approved seasoning Substances 0.000 description 2
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- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 2
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 description 2
- 244000061456 Solanum tuberosum Species 0.000 description 2
- 235000002595 Solanum tuberosum Nutrition 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 235000008429 bread Nutrition 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 150000001720 carbohydrates Chemical class 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000009477 fluid bed granulation Methods 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 235000021056 liquid food Nutrition 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 235000019629 palatability Nutrition 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 235000012015 potatoes Nutrition 0.000 description 2
- 235000008476 powdered milk Nutrition 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000012460 protein solution Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- PETSAYFQSGAEQY-UHFFFAOYSA-N ricinine Chemical compound COC=1C=CN(C)C(=O)C=1C#N PETSAYFQSGAEQY-UHFFFAOYSA-N 0.000 description 2
- 210000002966 serum Anatomy 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 108010011619 6-Phytase Proteins 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108010044091 Globulins Proteins 0.000 description 1
- 102000006395 Globulins Human genes 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
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- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
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- 235000015173 baked goods and baking mixes Nutrition 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 235000014510 cooky Nutrition 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
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- 239000003925 fat Substances 0.000 description 1
- 235000013355 food flavoring agent Nutrition 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 102000034238 globular proteins Human genes 0.000 description 1
- 108091005896 globular proteins Proteins 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000019426 modified starch Nutrition 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
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- 229940085127 phytase Drugs 0.000 description 1
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- 235000019685 rice crackers Nutrition 0.000 description 1
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Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J3/00—Working-up of proteins for foodstuffs
- A23J3/14—Vegetable proteins
- A23J3/16—Vegetable proteins from soybean
-
- 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
- A23L11/00—Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
- A23L11/05—Mashed or comminuted pulses or legumes; Products made therefrom
- A23L11/07—Soya beans, e.g. oil-extracted soya bean flakes
-
- 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
- A23L2/66—Proteins
-
- 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
- A23L33/185—Vegetable proteins
-
- 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
Definitions
- the present invention relates to a method for producing a low-hydratable 3-conglycinin protein, a low-hydratability, low-viscosity i3-conglycinin protein obtained by the method, and a food containing the same.
- conglycinin can be taken in various forms such as liquid foods such as drinks and soups, gel foods, dry or semi-dried foods such as bread and cookies, and tablet confections.
- the present inventors have repeatedly studied to improve the high hydration and high viscosity of the 3-conglycinin protein solution, and as a result, by heating the aqueous solution or paste of the protein under acidic conditions, Even if the ⁇ of the solution is returned to neutrality where the protein is originally soluble, the solubility is reduced.As a result, the high hydration and high viscosity of the 3-conglycinin protein are reduced over a wide ⁇ range, and the water is returned. Have been found to improve food quality and make it easier to process and ingest into various foods. The present inventors have conducted intensive studies on the heating conditions of the protein solution under acidic conditions, and have finally completed the present invention.
- the present invention is intended to reduce the solubility of protein by heating a solution containing 3-conglycinin protein under acidic conditions. And a process for producing a processed i3-conglycinin protein having low hydration and low viscosity. Further, the present invention relates to a processed 3-conglycinin protein obtained by the above method and a food containing the same.
- a process for producing processed-condaricinin protein which comprises heating a solution or paste containing 3-conglycinin protein under acidic conditions.
- a food roro comprising 3) conglycinin protein according to claim 4)
- i3-conglycinin substantially corresponds to 7S glopurin having a molecular weight ultracentrifugation sedimentation coefficient of 7S among globulin which is a generic name of soluble globular proteins of soybean.
- ⁇ -conglycinin usually consists of three types of subunits, but may be [3-conglycinin in which a part of the subunit is deleted].
- the amount of ⁇ -conglycinin it refers to the total amount of the 0 !, ', and ⁇ subunits that exist.
- 3-conglycinin protein refers to a protein containing ⁇ -conglycinin in an amount larger than that of a normal isolated protein. Normally, its purity exceeds 40% in the protein, and the higher the purity, the more efficient it is possible to ingest [3-conglycinin].
- the 3-conglycinin protein used in the present invention can be obtained by a fractionation method utilizing a difference in isoelectric point, such as the method of Thanh & Shibasaki (J. Agri Food Chem., 24, 117 1976) No. 124457), a fractionation method utilizing reactivity with calcium (JP-A-48-56843), a fractionation method utilizing a difference in solubility in ⁇ ⁇ ionic strength (JP-A-49-56843). 31843, JP-A-58-36345, JP-A-5-43597), and a fractionation method using a cold precipitation phenomenon and a reducing agent (JP-A-61-187755).
- the obtained one may be used. It is also possible to use breeding-obtained from soybeans rich in conglycinin / 3-conglycinin protein (Breeding Science, 50, 101, 2000 or US 6, 171, 640 B1).
- the solubility can be reduced by heating a solution or paste containing 3) -conglycinin protein under acidic conditions of pH 3.5 to 6.0. Outside this range, the solubility is insufficiently reduced, and the high hydration and high viscosity are not improved.
- the solubility is further reduced by heating in the pH range close to the isoelectric point of 3-condaricinin, pH 4.5-5.0. Therefore, although it depends on the heating temperature, heating at pH 3.8 to 5.8, especially at pH 4.0 to 5.6, results in reduced solubility of 3-) conglycinin protein.
- the optimal degree of solubility degradation depends on the food used.
- the heating temperature suitable for lowering the solubility depends on the pH, but may be a temperature higher than 75 ° C, preferably 85 ° C or higher, more preferably 95 ° C or higher. If the heating temperature is too low, it becomes difficult to improve the high hydration property. Heating at an excessively high temperature is not practical, and heating at a temperature higher than 160 ° C. may cause burning, which is not preferable. In addition, the decrease in solubility is greatly affected by factors such as pH and temperature, while the factor of heating time is small. However, in general, when the heating temperature is high, a short time is sufficient, When the heating temperature is low, it takes a long time.
- the concentration of the solution or base of 3] -conglycinin protein during heating is not particularly limited, but is preferably 5 to 20%, more preferably 5 to 15%, and still more preferably 5 to 10%. It is.
- concentration is high, agglomerates are formed by acidic heating. Agglomerates can be formed even at low concentrations. As it is, processing after acidic heating or processing into food may become difficult, so it is desirable to pulverize the agglomerates generated during acidic heating with a wet pulverizer or the like.
- the low-solubility i3-condaricinin protein obtained by drying may have coarse particles in some cases. May have a rough texture, so it is desirable to homogenize the solution with a high-pressure homogenizer or the like.
- the 3-conglycinin protein prepared by any of the methods described above is not heated under acidic conditions in this way, its dissolution rate (described later) in a neutral (PH 7.0) solution will be low. Although it has high hydration and high viscosity at 90% or more, the dissolution rate in a neutral (pH 7.0) solution is reduced to 70% or less due to heating under acidic conditions. A clear reduction in viscosity is observed.
- the solution or paste containing 3-chondaricinin protein obtained by the above treatment may be used as it is, or after being concentrated, neutralized, or sterilized. From the viewpoint of solubility and ease of use, it is practical to sterilize after neutralization and use as a low-soluble ⁇ -conglycinin protein dried using a drying device such as spray drying. You. However, if a solution or paste containing i3 -conglycinin with reduced solubility is heated above pH 6.0 and sterilized by heating at a high temperature, the solubility may increase slightly and hydration and viscosity may return. In such a case, taking into account that point, it is advisable to make a contrivance in advance such as heating under acidic conditions for lower solubility under stronger conditions.
- the ionic strength is adjusted to less than 0.2 by temporarily diluting with water or desalting, and the pH value is adjusted to 4.0 to 5.0.
- a so-called isoelectric point separation method for separating and recovering the insoluble fraction produced by the above method is exemplified, and then a form in which water is added, neutralized, heat sterilized, and dried is practical. Heating can be performed by a known HTST or UHT treatment.
- the solubility of the low-solubility 3-conglycinin protein obtained in the above treatment in a neutral (PH 7.0) solution is 70 or less, and it is necessary to select heating conditions as described above. As a result, it is possible to obtain less than 60%, less than 50%, or less than 40%, which can be used properly according to the application. If the dissolution rate is higher than 70%, the water reversion property is poor and the viscosity is high when processed into various foods or taken as foods, which is not preferable.
- the purity of ⁇ -condaricinin protein is not particularly limited,
- 3-conglycinin When the content is 40% or more, preferably 60% or more, and more preferably 70% or more, 3-conglycinin can be ingested or processed efficiently.
- the 3-conglycinin protein thus obtained can be used in various foods. For example, it can be used for evening tablets, powdered drinks, baked goods, flour or starch foods, and various premixes.
- the tablet is a powder mixture containing 3-conglycinin protein, or a granulated mixture of the mixture, and packed in a mold of a conventionally known tableting machine generally used for manufacturing tablets and the like. It can be obtained by shaping. Tablets can contain less than 80% by weight of 3_conglycinin protein, and if it exceeds 80% by weight, the hardness of the evening bullet will be insufficient, and cracks will soon occur, which is not preferable. In addition, for the purpose of ingesting i3-conglycinin, it is appropriate to contain 20% by weight or more, preferably 30% by weight or more, more preferably 40% by weight or more of -conglycinin protein.
- saccharides may be contained. Depending on the selection of saccharides, tablet confections with various hardness, texture and taste can be obtained. In addition, powdered milk, cocoa powder, juice powder, organic acids, flavorings, etc. can be added to the evening bullet to make tablet confections with excellent palatability, and emulsifiers, polysaccharides, and carbon dioxide to improve tableting properties. It is also possible to add silicon or the like.
- the tablet using the 3-conglycinin protein adheres to the teeth and becomes very hard to eat due to its high viscosity.
- the bulk specific gravity of j3-conglycinin protein is small, and when this powder is mainly used, the weight per tablet cannot be too large due to the relationship with the volume of the mill of the tableting machine.
- high hardness is required It requires a lot of pressure and is not very desirable on equipment.
- the bulk specific gravity of 3-conglycinin can be increased, and the adhesion to teeth when it is opened is suppressed, and the above-mentioned problems relating to workability and tablet quality are solved.
- Powdered beverages are obtained by mixing powder containing 3) -conglycinin protein with other raw material powders, and desirably granulating.
- powder soup, powdered miso soup, powdered coffee, etc. which are mainly used in combination with flavoring agents
- protein powder which is highly blended with 0-conglycinin protein.
- the content of 3-conglycinin protein is not particularly limited, but is preferably 20% by weight or more, preferably 30% by weight or more, and more preferably 40% by weight or more in order to efficiently take in 3-conglycinin. It is.
- 70% by weight or more of the raw material is preferable for the purpose of ingesting the protein itself.
- Powdered beverages include powders of vegetables, potatoes, beans, cereals, etc., powdered miso, powdered soy sauce, seasonings, fruit juice, powdered coffee, cocoa powder, powdered milk, sugar, starches, flavors, acidulants, etc. It can be used without limitation. If unprocessed 3-conglycinin protein is used, this formation is slightly improved by granulation, but it becomes more difficult to improve as the content increases. In particular, when the usage of the 3-conglycinin protein exceeds 50% by weight, it is difficult to obtain a sufficient dispersibility, and in some cases, the viscosity is increased by granulation. It is difficult.
- the rice cracker-like food is obtained by expanding the dough by heating or the like.
- the amount of jS-conglycinin protein should be at least 20% by weight, preferably at least 30% by weight, more preferably at least 40% by weight in the solid content.
- the texture and flavor can be satisfied.
- the content of) 3-conglycinin protein is suitably 90% by weight or less.
- Ingredients can be added with starchy substances, such as starches such as corn, waxy corn, potatoes, evening pio, wheat and rice, and their modified starches, or flours and oils such as wheat flour and rice flour, to enhance palatability. Can be improved.
- Spices and seasonings can also be added to season the dough.
- dough is prepared by adding water to such a powder mixture containing 3-conglycinin protein
- use of non-added i3-conglycinin protein results in the formation of a paste and the formation of a homogeneous dough.
- it is difficult to increase the mixing ratio to 50% by weight or more in the solid content.
- processed (3) -conglycinin protein it is difficult to form a cage, and mixing with a vertical mixer used for ordinary mixing is possible.
- the degree of swelling tends to be small for processed ones, and incomplete swelling may be too hard. In this case, replace the appropriate amount of processed 3-conglycinin protein with unprocessed one. 0
- Dissolution rate Adjust the pH of a 1% by weight aqueous solution of the sample to pH 7.0, and determine the ratio of the protein amount in the supernatant fraction centrifuged at 8,000 G for 5 minutes to the total protein amount in the aqueous solution by the Kjeldahl method.
- SDS-polyacrylamide electrophoresis Analyzed on a daradient gel with a gel concentration of 10-20% based on the method of Laemmli (Nature, 227, 6801970). The amount of protein applied is 5 g.
- Chromate oil A 50-fold mixture of formaldehyde and methanol (volume ratio, 2: 1) was added to the dry matter sample, and the fraction extracted at 160 ° C was weighed to obtain the chromata oil.
- SPE standard The electrophoresis pattern obtained by the above SDS-polyacrylamide electrophoresis was measured as an area by densitometry overnight, and the area ratio to the total area of the 3-conglycinin fraction was defined as the purity (SPE standard). And Here) 3-conglycinin content refers to the total amount of o ;, ', ⁇ -subunits.
- Example 3 Water is added to the precipitated phytate 3 -conglycinin protein precipitate curd prepared in the same manner as in Example 1 to homogenize it (solid content: 14.2%), and the pH is adjusted to 5.5 using caustic soda to 120 ° C. For 10 seconds. After that, the agglomerates generated were crushed using a commit roll (manufactured by URSCHEL LABORATRIES, INC.), The pH was adjusted to 6.0 using caustic soda, and sterilized by heating at 142 ° C for 7 seconds, and immediately spray-dried Thus, ⁇ -conglycinin protein powder was obtained. The 3-conglycinin purity of the obtained powder was 93%, and the solubility at ⁇ 7.0 was 34%.
- the precipitated curd of low phytic acid 3-conglycinin protein prepared in the same manner as in Example 1 was homogenized with 5 times the weight of water (solid content: 6.7), and the pH was adjusted to 5.5 using caustic soda. Heating was performed at ° C for 10 seconds. Then, the resulting aggregates are ground using a commit roll (made by URSCHEL LABORATRIES, IN), and the pH is adjusted to 6.0 using caustic soda. The solution was heat-sterilized at 142 ° C for 7 seconds, and immediately spray-dried to obtain ⁇ -chondaricinin protein powder ( ⁇ -1; dissolution rate at ⁇ 7.0 is 38%).
- the resulting mixture of 32 parts of ⁇ -1 and 68 parts of maltose was subjected to fluid bed granulation using 15 parts of a 0.2% by weight guar gum aqueous solution as a binder, followed by DKester F-20W (No. 3 parts, 1 part of powdered lemon juice, 0.5 part of powdered lemon flavor, and 1 part of citrate were added, and tablet confectionery having a diameter of 20 mm (1.7 g / particle) was prepared using a tableting machine.
- the obtained tablet confection had no problem in powder fluidity and moldability at the time of tableting, and had good adhesion with little to teeth even when eaten.
- the precipitated curd of low-phytic acid 3-conglycinin protein prepared in the same manner as in Example 1 was homogenized with 5 times the weight of water (solid content: 6.7%), and the pH was adjusted to 5.8 with caustic soda. Heat treatment was performed at 120 ° C for 10 seconds. Then, Agglomerates generated using a mitroll (URSCHEL LABORATRIES, IN) were powdered, and the solution was homogenized using a high-pressure homogenizer (150 kgf / cm 2 , manufactured by IZUMI FOOD MACHINERY CO., LTD.).
- T-2 3-conglycinin protein
- Example 5 rice cracker-like food
- the dough was made using T-1 and a 1: 1 mixture of T-1 and C-1 and produced a uniform dough, while the dough using C-1 produced many doughs and produced a uniform dough.
- the cloth using T-1 had a small expansion, while the cloth using a 1: 1 mixture of T-1 and C-1 expanded moderately.
- the texture the one using a 1: 1 mixture of T-1 and C-1 had a moderate crispy feeling and was the most preferable.
- those using T-1 became hard and did not have a very good texture. From the above results, it was shown that the use of processed (3) -conglycinin protein makes it easier to prepare the territory and to obtain a rice cracker-like food with a good texture.
- the present invention provides a soybean having improved high hydration property and high viscosity which is a problem when processed or ingested into various foods by heating a solution or paste containing soybean 3-conglycinin protein under acidic conditions.) 3-Conglycinin protein can be provided.
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- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Mycology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Biochemistry (AREA)
- Agronomy & Crop Science (AREA)
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- Coloring Foods And Improving Nutritive Qualities (AREA)
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Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE60330874T DE60330874D1 (de) | 2002-07-19 | 2003-07-22 | Bearbeitetes sojabohnen-conglycinin-protein |
AU2003304196A AU2003304196A1 (en) | 2002-07-19 | 2003-07-22 | PROCESSED SOYBEAN Beta-CONGLYCININ PROTEIN |
AT03741541T ATE454045T1 (de) | 2002-07-19 | 2003-07-22 | Bearbeitetes sojabohnen-conglycinin-protein |
EP03741541A EP1535517B1 (en) | 2002-07-19 | 2003-07-22 | Processed soybean beta-conglycinin protein |
US10/521,765 US7501492B2 (en) | 2002-07-19 | 2003-07-22 | Processed soybean β-conglycinin protein |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002211845A JP4380117B2 (ja) | 2002-07-19 | 2002-07-19 | 大豆7sたん白含有タブレット |
JP2002-211845 | 2002-07-19 |
Publications (1)
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WO2004110163A1 true WO2004110163A1 (ja) | 2004-12-23 |
Family
ID=31934930
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2003/009282 WO2004110163A1 (ja) | 2002-07-19 | 2003-07-22 | 加工された大豆βーコングリシニンたん白 |
Country Status (8)
Country | Link |
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US (1) | US7501492B2 (ja) |
EP (1) | EP1535517B1 (ja) |
JP (1) | JP4380117B2 (ja) |
CN (1) | CN100515221C (ja) |
AT (1) | ATE454045T1 (ja) |
AU (1) | AU2003304196A1 (ja) |
DE (1) | DE60330874D1 (ja) |
WO (1) | WO2004110163A1 (ja) |
Families Citing this family (7)
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CN100469257C (zh) * | 2002-11-12 | 2009-03-18 | 不二制油株式会社 | 分离大豆蛋白及其生产方法 |
JPWO2005092367A1 (ja) * | 2004-03-29 | 2008-02-07 | 不二製油株式会社 | アディポネクチン分泌促進組成物 |
BRPI0515936A (pt) * | 2004-09-29 | 2008-08-12 | Nestec Sa | proteìna globular ativada e seu uso em composições comestìveis |
JP4937109B2 (ja) * | 2005-02-24 | 2012-05-23 | 株式会社明治 | コラーゲンペプチド含有チュアブルタブレット及びその製造方法 |
JP5382840B2 (ja) * | 2005-08-23 | 2014-01-08 | 特定非営利活動法人プライメイト・アゴラ | サルモデルで薬効が確認された骨粗鬆症の予防又は治療剤 |
US20100303993A1 (en) * | 2007-12-27 | 2010-12-02 | Takayasu Motoyama | Novel soybean protein material and method for producing the same |
CN114304371A (zh) * | 2021-12-20 | 2022-04-12 | 东北农业大学 | 一种利用pH-偏移结合超声提高β-伴大豆球蛋白乳化性的方法 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11308969A (ja) * | 1998-04-28 | 1999-11-09 | Fuji Oil Co Ltd | 穀物タンパク質の製造方法 |
JP2002238442A (ja) * | 2000-12-14 | 2002-08-27 | Fuji Oil Co Ltd | 混合物、プレミックス、パンおよびパンの製造法 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0012485B1 (en) * | 1978-12-12 | 1983-11-09 | N.V. Safinco | Process for preparing a gel-forming protein product; gel-forming product and gel obtained by the process |
JPS5925650A (ja) | 1982-07-31 | 1984-02-09 | Fuji Oil Co Ltd | 粉状大豆蛋白の製造法 |
US6171640B1 (en) * | 1997-04-04 | 2001-01-09 | Monsanto Company | High beta-conglycinin products and their use |
KR100754051B1 (ko) | 2000-10-02 | 2007-08-31 | 후지 세이유 가부시키가이샤 | 분획된 대두 단백질 및 그 제조법 |
-
2002
- 2002-07-19 JP JP2002211845A patent/JP4380117B2/ja not_active Expired - Fee Related
-
2003
- 2003-07-22 US US10/521,765 patent/US7501492B2/en not_active Expired - Fee Related
- 2003-07-22 WO PCT/JP2003/009282 patent/WO2004110163A1/ja active Application Filing
- 2003-07-22 CN CNB03822349XA patent/CN100515221C/zh not_active Expired - Fee Related
- 2003-07-22 EP EP03741541A patent/EP1535517B1/en not_active Expired - Lifetime
- 2003-07-22 AU AU2003304196A patent/AU2003304196A1/en not_active Abandoned
- 2003-07-22 DE DE60330874T patent/DE60330874D1/de not_active Expired - Fee Related
- 2003-07-22 AT AT03741541T patent/ATE454045T1/de not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11308969A (ja) * | 1998-04-28 | 1999-11-09 | Fuji Oil Co Ltd | 穀物タンパク質の製造方法 |
JP2002238442A (ja) * | 2000-12-14 | 2002-08-27 | Fuji Oil Co Ltd | 混合物、プレミックス、パンおよびパンの製造法 |
Non-Patent Citations (4)
Title |
---|
NAGANO T. ET AL.: "Dynamic viscoeleastic study on the gelation properties of beta-conglycinin-rich and glycinin-rich soybean protein isolates", J. AGRIC. FOOD CHEM., vol. 44, no. 11, 1996, pages 3484 - 3488, XP002073720 * |
PETRUCCELLI S. ET AL.: "Soy protein isolate components and their interactions", J. AGRIC. FOOD CHEM., vol. 43, no. 7, 1995, pages 1762 - 1767, XP000514045 * |
PUPPO M.C. ET AL.: "Structural properties of heat-induced soy protein gels as affected by ionic strength and pH", J. AGRIC. FOOD CHEM., vol. 46, no. 9, 1998, pages 3583 - 3589, XP002973990 * |
RENKEMA J.M.S. ET AL.: "The effect of pH on heat denaturation and gel forming properties of soy proteins", JOURNAL OF BIOTECHNOLOGY, vol. 79, no. 3, 2000, pages 223 - 230, XP004201986 * |
Also Published As
Publication number | Publication date |
---|---|
EP1535517A1 (en) | 2005-06-01 |
AU2003304196A1 (en) | 2005-01-04 |
CN100515221C (zh) | 2009-07-22 |
JP4380117B2 (ja) | 2009-12-09 |
EP1535517A4 (en) | 2005-11-16 |
ATE454045T1 (de) | 2010-01-15 |
JP2004049124A (ja) | 2004-02-19 |
DE60330874D1 (de) | 2010-02-25 |
EP1535517B1 (en) | 2010-01-06 |
US20050175766A1 (en) | 2005-08-11 |
CN1681394A (zh) | 2005-10-12 |
US7501492B2 (en) | 2009-03-10 |
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