WO2004078334A1 - 多糖と蛋白質との複合体を有効成分とする乳化剤およびその製造方法ならびに乳化組成物 - Google Patents
多糖と蛋白質との複合体を有効成分とする乳化剤およびその製造方法ならびに乳化組成物 Download PDFInfo
- Publication number
- WO2004078334A1 WO2004078334A1 PCT/JP2004/002669 JP2004002669W WO2004078334A1 WO 2004078334 A1 WO2004078334 A1 WO 2004078334A1 JP 2004002669 W JP2004002669 W JP 2004002669W WO 2004078334 A1 WO2004078334 A1 WO 2004078334A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- emulsifier
- protein
- acidic
- polysaccharide
- saccharide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
- C09K23/16—Amines or polyamines
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
- C09K23/30—Proteins; Protein hydrolysates
Definitions
- Emulsifier comprising complex of polysaccharide and protein as active ingredient, method for producing the same, and emulsified composition
- the present invention relates to an emulsifier. More specifically, an emulsifier having improved functions, which is obtained by heating a polysaccharide containing an acidic saccharide having a carboxylic acid group as a constituent saccharide and a protein or protein hydrolyzate under acidic conditions, and a method for producing the same, are provided.
- the present invention also relates to an emulsified composition using the emulsifier.
- emulsifiers can be broadly classified into monomolecular emulsifiers and polymer emulsifiers.
- the monomolecular emulsifier is a so-called surfactant, and examples thereof include fatty acid stone / glycerin fatty acid ester, sucrose fatty acid ester, polyoxyethylene sorbitan fatty acid ester, and the like.
- Polymeric emulsifiers include natural products such as gum arabic and casein, or synthetic products such as atalylate and polypinyl alcohol.
- emulsifiers may be used alone depending on the application, or they may be used in an appropriate blend.However, monomolecular emulsifiers are generally vulnerable to changes in H, and are not sensitive to changes in concentration due to addition or dilution of salts. This leaves a problem that the emulsifiability is lost. In addition, the use of these synthetic monomolecular emulsifiers tends to be disliked, reflecting the recent health consciousness. On the other hand, there are also natural polymers with emulsifying power. But weak emulsifying power, high viscosity impairs the texture or physical properties of food
- Proteins such as soybeans, wheat, milk, and hen's eggs have been widely used in food processing because of their functional properties of emulsification, foaming and water retention.
- many proteins can be weakly acidic at pH 4 to 6, weakening the negative charge of the protein and reducing the repulsion between protein molecules, resulting in reduced solubility and consequently reduced functional properties.
- milk proteins such as soy protein and casein, have a markedly reduced solubility under weakly acidic conditions and form precipitates, which lowers the emulsifying power.
- Many foods are weakly acidic and do not efficiently utilize the functional properties of proteins.
- Patent Document 2 Japanese Patent Application Laid-Open No. 6-112192.
- the water-soluble soybean polysaccharide extracted at a high temperature with a weakly acidic pH near the isoelectric point of soybean protein at pH 4.5 which is exemplified as a suitable condition here, does not always have sufficient emulsifying power.
- the emulsifier could be emulsified only up to 4 times the weight of the emulsifier in terms of the weight ratio of the emulsifier, and the range of use was limited.
- various studies have been made to impart new functions by complexing saccharides and proteins.
- An object of the present invention is to provide an emulsifier having high safety and improved functional activity, a process for producing the same, and an emulsified composition using the emulsifier.
- the present inventors have conducted intensive studies to solve the above problems, and as a result, reconfirmed that the dehydration condensation reaction of a compound having a lipoxyl group and a compound having an amino group also proceeds in an aqueous system. In addition, it was found that by adjusting this reaction system to a specific pH, the reactivity was dramatically improved, and the emulsifying ability of the complex obtained by the reaction was enhanced. Issued.
- the present invention has been completed based on such findings. You. That is, the present invention provides an acid produced by heating a polysaccharide containing an acidic saccharide having a lipoxyl group as a constituent saccharide and a protein or protein hydrolyzate under an acidic condition of PH 2 to PH 5.
- an emulsifier containing a polysaccharide-protein complex as an active ingredient provides an acidic polysaccharide comprising heating a polysaccharide containing an acidic saccharide having a hydroxyl group as a constituent saccharide and a protein or a proteolysate under an acidic condition of pH 2 to 5.
- Examples of the acidic sugar having a hydroxyl group according to the present invention include carboxylic acids such as galacturonic acid, glucuronic acid and mannuronic acid, and carboxymethyl etherified glucose. And sulphonic acid etherified sugars.
- Polysaccharides containing these as constituent sugars include, for example, natural polysaccharides such as vectin, alginic acid, and arabic gum; fermented polysaccharides such as dielan gum; lipoxymethyl cellulose; Examples thereof include synthetic polysaccharides such as alginic acid propylene glycol ester, and acidic oligosaccharides such as degraded products of alginate and alginic acid.
- the hydroxyl group may be in a free or salt state, but is preferably present in a state in which alcohols such as methyl alcohol are ester-bonded. In addition, it is preferable that at least 50% of the hydroxyl group is esterified. If the degree of esterification is 50% or less, Depending on the pH and the presence of salts, gelation may occur and the reactivity may be reduced. There is no particular upper limit on the degree of esterification that is appropriate for use, but the degree of esterification of natural polysaccharides is usually up to about 80%. The higher the content of acidic sugars in the carbohydrate, the better, but preferably more than 10% by weight, more preferably more than 20% by weight, and more preferably more than 30% by weight. Is preferred, and there is no particular upper limit.
- proteins include plant-derived proteins such as soybean protein, corn protein, wheat protein, endogenous bean protein, as well as casein, egg white albumin, and whey.
- Animal proteins such as protein, gelatin, actin myosin, and silk protein may be used, and hydrolysates of proteins such as polypeptides, peptides, and amino acids. It is OK.
- Polysaccharides and proteins containing acidic sugars having a lipoxyl group as constituent sugars can be used either in a water-soluble state or in an insoluble state.
- the appropriate ratio for obtaining a complex of a protein and a polysaccharide containing an acidic saccharide having a carboxyl group ′ as a constituent saccharide is from 100: 1 to 1:20 for acidic polysaccharide: protein. It is preferably 50: 1 to 1:10, more preferably 10: 1 to 1: 2.
- the complex is produced by mixing a polysaccharide containing an acidic saccharide having a lipoxyl group as a constituent saccharide and a protein in an aqueous system and then heating the mixture.
- a polysaccharide containing an acidic saccharide having a lipoxyl group as a constituent saccharide and a protein in an aqueous system and then heating the mixture.
- the raw material is suspended in an aqueous solution or water, and After adjusting the temperature, heat and separate the water-soluble fraction and dry it as it is.
- aqueous solution or water For example, after neutralizing the heated solution, dialysis treatment, activated carbon treatment, resin adsorption treatment, or ethanol
- inorganic precipitation hydrophobic substances or low-molecular substances by subjecting it to a Knoll precipitation treatment, etc., it is dried and then dried.
- a polysaccharide-protein complex containing as a constituent sugar can be obtained.
- Heating is performed at pH 2 to 5 and preferably at pH 3 to 4. If the pH is lower than 2, it is not preferable because decomposition, which is a side reaction during the complexation reaction, is promoted. When the pH exceeds 5, the reactivity is remarkably reduced.
- the acid used at this time is not particularly limited, but when it is intended as an emulsifier for food use, it is used in the food industry, including hydrochloric acid, phosphoric acid, sulfuric acid, lactic acid, citric acid, oxalic acid, etc. Can be used.
- the heating temperature during the reaction is preferably at least 80, preferably more than 100 ° C, at least 105, and more preferably at least 120. Generally, it is sufficient to heat under pressure while not dissolving or dispersing in water, or in a wet or pasted state.
- the upper limit of the heating temperature is not particularly specified, but when the temperature is extremely high, a side reaction occurs and coloring becomes easy. Usually, it is performed at 180 ° C or lower, preferably at 150 ° C or lower.
- the emulsifier according to the present invention containing a polysaccharide-protein complex containing an acidic saccharide having a lipoxyl group as a constituent saccharide as an active ingredient is a so-called emulsifier in comparison with individual acidic saccharide-containing saccharides and proteins before the reaction.
- Functions of what is called Be improved or newly granted For example, levels of emulsifying power and emulsifying stabilizing ability not found in individual polysaccharides or proteins before the reaction, as well as improving physical properties of flour products, stabilizing dispersion, foaming, stabilizing foam, Functions such as water retention are expressed by the formation of the complex.
- fragrances By utilizing these functional activities, emulsified fragrances, foods such as mayonnaise, dressing or creams, cosmetics such as hand creams, and coatings It can be widely used in the general living industry represented by medicines such as repellents and pesticides such as insecticides.
- the method of evaluating the emulsifying ability used as an indicator of the functional activity of the emulsifier containing the polysaccharide-protein complex as an active ingredient in the present invention is as follows.
- Soybean oil is added to 100 g of a 5% aqueous solution, and judgment is made based on the amount added until phase inversion. When the product of the present invention is used, the weight ratio of the oil / complex becomes 5 or more.
- the emulsification conditions when adding soybean oil shall be homogenization with a homomixer ( ⁇ K homomixer; Tokushu Kika Kogyo Co., Ltd.) with vigorous stirring at 1000 rpm.
- the product of the present invention can be used alone as an emulsifier, but by using it in combination with an existing emulsifier, the disadvantages of the existing emulsifier can be compensated.
- Existing monomolecular emulsifiers include various anionic surfactants typified by fatty acid stones, cationic surfactants such as quaternary ammonium salts, glycerin fatty acid esters, and sucrose fatty acids.
- Nonionic surfactants such as esters, polyoxyethylene sorbitan fatty acid esters, and both lecithin Surfactants and the like.
- existing polymer emulsifiers include natural emulsifiers, for example, agar, carrageenan, phaceleran, tamarin seed polysaccharide, and water-soluble soy polysaccharide.
- natural emulsifiers for example, agar, carrageenan, phaceleran, tamarin seed polysaccharide, and water-soluble soy polysaccharide.
- albumin such as rubiagum, gelatin, whey, casein sodium, various starches, and the like.
- Semi-synthetic pastes include carboxymethylcellulose (CMC), methylcellulose (MC), hydroxyxethylcellulose (HEC), propylene glycol 7-luginate, and the like.
- Modified starch typified by luster and soluble starch can be exemplified, and examples of the synthetic paste include polyvinyl alcohol and sodium polyacrylate.
- the effect of the emulsifier in the present invention may be further improved by using one or more of the above-mentioned various emulsifiers in combination, and the emulsifier can make up for the drawbacks of the various emulsifiers.
- sugars such as sucrose and starch syrup
- polyvalent alcohols such as glycerin, D-sorbitol, propylene glycol, and the like
- Stability may be improved by adding an acidulant such as lactic acid, vinegar, citric acid, and phosphoric acid.
- additives such as anti-fading agents and preservatives such as L-ascorbic acid, its derivatives, and aminocarbonyl reaction products can be added.
- angiotensin II 0.5 mg is dissolved in 1501 lOOmM tartrate Na_HC1 buffer (pH 5.0) and heated at 120 ° C for 90 minutes. I did. The reaction product generated after the heating was separated by reverse-phase HPLC to recover the reaction compound. Subsequently, the structure was confirmed by mass spectral analysis of the recovered reaction compound. As shown in the results in Fig. 1, the results of mass spectral analysis indicate that tartaric acid contained in the buffer was amide-bound to the N-terminal of angiotensin II. Was confirmed.
- angiotensin II was added to 1501 lOOmM tartaric acid-HC1 buffer (pH 2.0), lOOmmM tartaric acid Na-HC1 buffer (pH 3 PH 7.0), 100 mM Tartrate Na-NaOH buffer solution (pH 9.0, pHIO. 0), and dissolved at 120 ° C. Heating was performed for 90 minutes. The reaction product generated after the heating was separated by reversed-phase HPLC, and the reaction compound was quantified. As shown in the results in Fig. 2, the results of the quantitative analysis confirmed that the reaction products increased dramatically between pH 2 and pH 5, with pH 3.0 as the center. It was done.
- TypeUSP-H Esterification degree 70.5; Sansho Co., Ltd. 200 g and soy protein (trade name“ Fujipro-E ”; Fuji Oil Co., Ltd.) 100 g with warm water 5
- the pH was adjusted to 3.0 with hydrochloric acid, and the mixture was heated at 120 for 1.5 hours to produce a heated product of HM-vector and soybean protein.
- the mixture was cooled to room temperature, centrifuged (100,000 G ⁇ 30 minutes), and the supernatant was dried to collect 25 g of a solid. This solid was converted to a 5% aqueous solution, and emulsified with a homomixer at 100,000 rpm while adding soybean oil. The phase was inverted when 250 g of soybean oil was added. The oil / composite weight ratio at this time was 50.
- the pH was adjusted to 4.0 with hydrochloric acid, and the mixture was heated at 120 for 1.5 hours to produce a heated product of HM-vector and soybean protein.
- the mixture was cooled to room temperature, centrifuged (100,000 GX for 30 minutes), and the supernatant was dried to collect 202.5 g of a solid. This solid was converted to a 5% aqueous solution, and soybean oil was added thereto using a homomixer.
- the emulsification treatment was performed at 0.000 rpm, the phase was inverted when 12 Og of soybean oil was added to 100 g of an aqueous solution.
- the oil / composite weight ratio at this time was 24.
- the pH was adjusted to 2.0 with hydrochloric acid, and the mixture was heated at 120 for 1.5 hours to produce a heated product of HM-pectin and soybean protein. After heating, the mixture was cooled to room temperature, centrifuged (100,000 G ⁇ 30 minutes), and the supernatant was dried to recover 243 g of a solid.
- the solid was converted to a 5% aqueous solution, and emulsified at 100 000 rpm with a homomixer while adding soybean oil to give 100 g of an aqueous solution.
- the phase was inverted when 60 g of soybean oil was added.
- the oil / composite weight ratio at this time was 12.
- the pH was adjusted to 5.0 with caustic soda, and the mixture was heated at 120 ° C for 1.5 hours to produce a heated product of HM-pectin and soybean protein.
- the mixture was cooled to room temperature, centrifuged (1000 GX 30 minutes), and the supernatant was dried. 184 g of a solid was recovered.
- this solid was converted to a 5% aqueous solution and emulsified with a homomixer at lOOO rpm while adding soybean oil.
- the phase was inverted when 45 g of soybean oil was added.
- the oil / composite weight ratio at this time was 9.
- the solid was converted to a 5% aqueous solution, and emulsified at 100 rpm with a homomixer while adding soybean oil to obtain a 100 g aqueous solution.
- the phase was inverted when 5 g of soybean oil was added to the mixture.
- the oil / composite weight ratio at this time was 1.
- the solid was converted to a 5% aqueous solution, and emulsified with a homomixer at l OOOO rpm while adding soybean oil.
- the phase was inverted when 15 g of soybean oil was added.
- the oil / composite weight ratio at this time was 3.
- soybean protein (trade name “Fujipro-E”; manufactured by Fuji Oil Co., Ltd.) was dissolved in 800 g of warm water, and the pH was adjusted to 3.0 with hydrochloric acid. The mixture was heated at 0 to 1.5 hours to obtain a thermally decomposed product of soybean protein. After heating, the mixture was cooled to room temperature, centrifuged (100,000 GX for 30 minutes), and the supernatant was dried to recover 11 g of a solid. Also, this solid When the mold was emulsified with a homomixer at 100,000 rpm while adding soybean oil to a 5% aqueous solution, 100 g of the aqueous solution was reconstituted. The phase was inverted when 22 g of soybean oil was added. The oil / composite weight ratio at this time was 4.4.
- Comparative Example 3 and The decomposed product obtained in Comparative Example 4 was mixed at a weight ratio of 2: 1 to form a 5% aqueous solution, and the mixture was mixed with a homomixer while adding soybean oil.
- the emulsification treatment was performed at 0.000 rpm, the phase inversion occurred when 12 g of soybean oil was added to 100 g of the aqueous solution.
- the oil / composite weight ratio at this time was 2.4.
- Warm water was added to the mixture so that the solid content concentration became 5%, and the mixture was heated at pH 4.0 and 105 for 180 minutes.
- the product of the present invention 4 obtained by performing the same treatment as in Example 1 And 2 parts of sodium caseinate were dissolved in 69 parts of water, and 0.1 part of a commercially available Milk Flavor (“Milk FT-013”, manufactured by Takasago International Inc.) was added.
- the meringue confectionery produced in this way shows a stable bubble state, there is little change over time during the squeezing operation, and the texture of each meringue confectionery is stable. Was. In addition, there was almost no structural destruction due to firing, and the texture after firing was fine and good.
- LM-1 vector (trade name: LM-SN 325 J Esterification degree 24; Snow Brand Foods Co., Ltd.) 200 g and soy protein (trade name “Fujipro-E”; Fuji Oil Co., Ltd.) 1
- the solution was gelled when the pH was adjusted to 3.0 with hydrochloric acid.
- 900 g of hot water was further added to dilute and dissolve the gel, and the mixture was heated at 120 for 1.5 hours to produce a heated product of LM-pectin and soy protein.
- the mixture was cooled to room temperature, centrifuged (100,000 G ⁇ 30 minutes), and the supernatant was dried to collect a solid.
- this solid was prepared as a 5% 7) solution, and the soybean oil was added thereto, and the mixture was subjected to a milk mixing process at 100,000 rpm with a homomixer. The phase was inverted when 52 g of soybean oil was added to the aqueous solution of 1 g. The oil / composite weight ratio at this time was 10.4.
- the complex obtained by the production method of the present invention in which a polysaccharide containing an acidic saccharide having a lipoxyl group as a constituent saccharide and a protein or protein hydrolyzate is heated under acidic conditions of pH 2 to 5 is different from a conventional conjugate as an emulsifier.
- This is an emulsifier with significantly improved emulsifying activity, and is advantageously used in the production of emulsions containing a large amount of fats and oils relative to the amount of emulsifier.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- General Preparation And Processing Of Foods (AREA)
- Medicinal Preparation (AREA)
- Cosmetics (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
Description
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005503079A JPWO2004078334A1 (ja) | 2003-03-04 | 2004-03-03 | 多糖と蛋白質との複合体を有効成分とする乳化剤およびその製造方法ならびに乳化組成物 |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003057843 | 2003-03-04 | ||
| JP2003-057843 | 2003-03-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2004078334A1 true WO2004078334A1 (ja) | 2004-09-16 |
Family
ID=32958774
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2004/002669 Ceased WO2004078334A1 (ja) | 2003-03-04 | 2004-03-03 | 多糖と蛋白質との複合体を有効成分とする乳化剤およびその製造方法ならびに乳化組成物 |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPWO2004078334A1 (ja) |
| WO (1) | WO2004078334A1 (ja) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007026090A1 (de) | 2007-06-04 | 2008-12-24 | Friedrich-Schiller-Universität Jena | Proteine und Polysaccharide enthaltende Emulsion für Lebensmittel sowie deren Herstellung und Verwendung |
| EP2196097A1 (en) | 2008-12-04 | 2010-06-16 | Nestec S.A. | Hydrolysed protein-polysaccharide complexes |
| CN101743747B (zh) * | 2008-06-17 | 2012-05-02 | 索尼计算机娱乐公司 | 信息处理装置 |
| JP2012187099A (ja) * | 2011-02-21 | 2012-10-04 | Shinshu Univ | フェルラ酸結合型糖質及びその製造方法 |
| EP1935258B1 (en) * | 2005-10-14 | 2013-02-13 | Knorr Foods Co., Ltd. | W1/o/w2-type double emulsion dressing and method for production thereof |
| WO2017170505A1 (ja) * | 2016-03-30 | 2017-10-05 | 不二製油グループ本社株式会社 | 高耐熱性付与用乳化安定剤及びその製造方法 |
| WO2019087666A1 (ja) * | 2017-11-02 | 2019-05-09 | 三栄源エフ・エフ・アイ株式会社 | 水溶性又は水分散性微粒子の製造方法、乳化機能代替物としての使用又は使用方法、乳化物の製造方法、食品の製造方法及び乳化物を含む食品 |
| CN116369496A (zh) * | 2023-04-13 | 2023-07-04 | 东北农业大学 | 一种利用阿拉伯胶增强大豆蛋白原纤维乳化特性的方法 |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01233300A (ja) * | 1988-03-15 | 1989-09-19 | Wako Pure Chem Ind Ltd | 機能性蛋白質 |
| JPH03215498A (ja) * | 1990-01-12 | 1991-09-20 | Nakano Vinegar Co Ltd | 蛋白質―多糖類複合体 |
| JPH07258292A (ja) * | 1994-03-25 | 1995-10-09 | Dainippon Pharmaceut Co Ltd | 蛋白質−キシログルカン複合体 |
| JPH10262560A (ja) * | 1997-03-28 | 1998-10-06 | Kao Corp | 乳化組成物及びその製造法 |
| WO1999062935A1 (en) * | 1998-06-01 | 1999-12-09 | Fuji Oil Co., Ltd. | Reaction products between carboxylic acid and amino acid or amino acid condensate and process for producing the same |
| JP2001046851A (ja) * | 1999-08-12 | 2001-02-20 | Fuji Oil Co Ltd | 乳化剤組成物及びこれを用いた酸性水中油型乳化物 |
| JP2002363197A (ja) * | 2001-06-07 | 2002-12-18 | Asahi Denka Kogyo Kk | タンパク質・糖質複合組成物 |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4250776B2 (ja) * | 1996-12-05 | 2009-04-08 | 不二製油株式会社 | 糖質−蛋白質複合体およびその製造法 |
| JP2002330710A (ja) * | 2001-02-20 | 2002-11-19 | Fuji Oil Co Ltd | 分散安定剤の製造方法及び分散安定化された製品 |
-
2004
- 2004-03-03 WO PCT/JP2004/002669 patent/WO2004078334A1/ja not_active Ceased
- 2004-03-03 JP JP2005503079A patent/JPWO2004078334A1/ja active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01233300A (ja) * | 1988-03-15 | 1989-09-19 | Wako Pure Chem Ind Ltd | 機能性蛋白質 |
| JPH03215498A (ja) * | 1990-01-12 | 1991-09-20 | Nakano Vinegar Co Ltd | 蛋白質―多糖類複合体 |
| JPH07258292A (ja) * | 1994-03-25 | 1995-10-09 | Dainippon Pharmaceut Co Ltd | 蛋白質−キシログルカン複合体 |
| JPH10262560A (ja) * | 1997-03-28 | 1998-10-06 | Kao Corp | 乳化組成物及びその製造法 |
| WO1999062935A1 (en) * | 1998-06-01 | 1999-12-09 | Fuji Oil Co., Ltd. | Reaction products between carboxylic acid and amino acid or amino acid condensate and process for producing the same |
| JP2001046851A (ja) * | 1999-08-12 | 2001-02-20 | Fuji Oil Co Ltd | 乳化剤組成物及びこれを用いた酸性水中油型乳化物 |
| JP2002363197A (ja) * | 2001-06-07 | 2002-12-18 | Asahi Denka Kogyo Kk | タンパク質・糖質複合組成物 |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1935258B1 (en) * | 2005-10-14 | 2013-02-13 | Knorr Foods Co., Ltd. | W1/o/w2-type double emulsion dressing and method for production thereof |
| DE102007026090A1 (de) | 2007-06-04 | 2008-12-24 | Friedrich-Schiller-Universität Jena | Proteine und Polysaccharide enthaltende Emulsion für Lebensmittel sowie deren Herstellung und Verwendung |
| CN101743747B (zh) * | 2008-06-17 | 2012-05-02 | 索尼计算机娱乐公司 | 信息处理装置 |
| EP2196097A1 (en) | 2008-12-04 | 2010-06-16 | Nestec S.A. | Hydrolysed protein-polysaccharide complexes |
| AU2009324245B2 (en) * | 2008-12-04 | 2014-11-20 | Nestec S.A. | Hydrolysed protein-polysaccharide complexes |
| JP2012187099A (ja) * | 2011-02-21 | 2012-10-04 | Shinshu Univ | フェルラ酸結合型糖質及びその製造方法 |
| WO2017170505A1 (ja) * | 2016-03-30 | 2017-10-05 | 不二製油グループ本社株式会社 | 高耐熱性付与用乳化安定剤及びその製造方法 |
| WO2019087666A1 (ja) * | 2017-11-02 | 2019-05-09 | 三栄源エフ・エフ・アイ株式会社 | 水溶性又は水分散性微粒子の製造方法、乳化機能代替物としての使用又は使用方法、乳化物の製造方法、食品の製造方法及び乳化物を含む食品 |
| CN111163859A (zh) * | 2017-11-02 | 2020-05-15 | 三荣源有限公司 | 水溶性或水分散性微粒的制造方法、作为乳化功能替代物的用途或使用方法、乳化物的制造方法、食品的制造方法和包含乳化物的食品 |
| JPWO2019087666A1 (ja) * | 2017-11-02 | 2020-12-24 | 三栄源エフ・エフ・アイ株式会社 | 水溶性又は水分散性微粒子の製造方法、乳化機能代替物としての使用又は使用方法、乳化物の製造方法、食品の製造方法及び乳化物を含む食品 |
| JP7213189B2 (ja) | 2017-11-02 | 2023-01-26 | 三栄源エフ・エフ・アイ株式会社 | 水溶性又は水分散性微粒子の製造方法、乳化機能代替物としての使用又は使用方法、乳化物の製造方法、食品の製造方法及び乳化物を含む食品 |
| US12376613B2 (en) | 2017-11-02 | 2025-08-05 | San-Ei Gen F.F.I., Inc. | Method for producing water-soluble or water-dispersible microparticles, use or method for use as substitute having emulsifying function, method for producing emulsion, method for producing food and food containing emulsion |
| CN116369496A (zh) * | 2023-04-13 | 2023-07-04 | 东北农业大学 | 一种利用阿拉伯胶增强大豆蛋白原纤维乳化特性的方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPWO2004078334A1 (ja) | 2006-06-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6455090B1 (en) | Liquid additive for thickener | |
| AU2006299642B2 (en) | Stabilizers and compositions and products comprising same | |
| JP5321028B2 (ja) | 食品用物性改良剤 | |
| JP3874560B2 (ja) | 微細セルロース含有複合物 | |
| JP6724104B2 (ja) | 大麦粉末を含む食品 | |
| JP5627284B2 (ja) | 乳化型ドレッシング | |
| CN107531940A (zh) | 纤维素复合体 | |
| JP4117818B2 (ja) | 崩壊性セルロース含有食品組成物 | |
| JP4044128B1 (ja) | タンパク質含有液状組成物用増粘化剤 | |
| WO2004078334A1 (ja) | 多糖と蛋白質との複合体を有効成分とする乳化剤およびその製造方法ならびに乳化組成物 | |
| JPH1014494A (ja) | 酸性飲食品、酸性飲食品用酸性クリームおよび粉末 | |
| JP5136467B2 (ja) | 卵白用起泡性向上剤 | |
| JP3905833B2 (ja) | 増粘用添加物 | |
| JPH06121922A (ja) | 乳化剤及び乳化組成物 | |
| EP1929881B1 (en) | Emulsion composition and method of preparing the same | |
| JP3506936B2 (ja) | セルロース含有複合体 | |
| JPH1146722A (ja) | セルロース含有複合体 | |
| US6987182B2 (en) | Process for producing cold-gelling hydrocolloids | |
| JP3665010B2 (ja) | 微細セルロース含有複合体を配合してなる食品組成物 | |
| JP5644211B2 (ja) | 酸性水中油型乳化食品 | |
| JP2002363197A (ja) | タンパク質・糖質複合組成物 | |
| JP4035390B2 (ja) | 液状食品素材及びその製造方法 | |
| JP3437270B2 (ja) | 水中油型乳化食品 | |
| JP4616215B2 (ja) | タンパク質含有液状組成物用増粘化剤 | |
| JP2006014629A (ja) | 粉末油脂組成物 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| WWE | Wipo information: entry into national phase |
Ref document number: 2005503079 Country of ref document: JP |
|
| 122 | Ep: pct application non-entry in european phase |