[go: up one dir, main page]

JP6771335B2 - Method for producing soy protein for food composition and method for producing food composition - Google Patents

Method for producing soy protein for food composition and method for producing food composition Download PDF

Info

Publication number
JP6771335B2
JP6771335B2 JP2016161419A JP2016161419A JP6771335B2 JP 6771335 B2 JP6771335 B2 JP 6771335B2 JP 2016161419 A JP2016161419 A JP 2016161419A JP 2016161419 A JP2016161419 A JP 2016161419A JP 6771335 B2 JP6771335 B2 JP 6771335B2
Authority
JP
Japan
Prior art keywords
soybean protein
dispersion
producing
liquid
food composition
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.)
Active
Application number
JP2016161419A
Other languages
Japanese (ja)
Other versions
JP2018027066A (en
Inventor
卓 村松
卓 村松
和光 大坪
和光 大坪
美子 廣田
美子 廣田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Meiji Co Ltd
Original Assignee
Meiji Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Meiji Co Ltd filed Critical Meiji Co Ltd
Priority to JP2016161419A priority Critical patent/JP6771335B2/en
Publication of JP2018027066A publication Critical patent/JP2018027066A/en
Application granted granted Critical
Publication of JP6771335B2 publication Critical patent/JP6771335B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • General Preparation And Processing Of Foods (AREA)

Description

本発明は、食品組成物用の大豆たんぱく質の製造方法及び食品組成物の製造方法に関する。 The present invention relates to a method for producing soybean protein for a food composition and a method for producing a food composition.

乳化組成物である流動食の窒素源としては、一般に、乳由来のたんぱく質と大豆由来のたんぱく質が利用され、近年、大豆たんぱく質は、その栄養価、機能性、経済性、環境性等が注目されている。
大豆たんぱく質は、脱脂大豆をアルカリ溶液で抽出し、不溶成分を遠心分離により除去し、酸性下でたんぱく質を沈殿させた後、遠心分離により得たカード状のたんぱく質を水洗、乾燥して、製造することができる。
Milk-derived proteins and soybean-derived proteins are generally used as nitrogen sources for liquid foods, which are emulsified compositions. In recent years, soybean proteins have been attracting attention for their nutritional value, functionality, economy, and environmental friendliness. ing.
Soybean protein is produced by extracting defatted soybeans with an alkaline solution, removing insoluble components by centrifugation, precipitating the protein under acidic conditions, and then washing and drying the curd-shaped protein obtained by centrifugation with water. be able to.

しかし、製造過程の処理により、たんぱく質の立体構造が変化し、たんぱく質表面が疎水性基となり、水への分散性が悪く(例えば、非特許文献1を参照)、脂質を加えた際に乳化が難しいという問題がある。 However, due to the treatment in the manufacturing process, the three-dimensional structure of the protein changes, the surface of the protein becomes a hydrophobic group, the dispersibility in water is poor (see, for example, Non-Patent Document 1), and emulsification occurs when a lipid is added. There is a problem that it is difficult.

大豆たんぱく質を食品組成物に用いた例として、特許文献1には、大豆たん白原料の水溶液または水分散液を亜硫酸塩の存在下にpH5.7〜7.4、110℃〜160℃で加熱処理して得られた大豆たん白素材を用いた濃厚流動食が開示されている。また、特許文献2には、大豆蛋白素材、第二族元素化合物及び分散剤を含有する濃厚流動食が開示されている。 As an example of using soybean protein in a food composition, Patent Document 1 states that an aqueous solution or an aqueous dispersion of a soybean protein raw material is heated at pH 5.7 to 7.4 and 110 ° C to 160 ° C in the presence of sulfites. A concentrated liquid food using a soybean protein material obtained by treatment is disclosed. Further, Patent Document 2 discloses a concentrated liquid food containing a soybean protein material, a group II element compound and a dispersant.

国際公開第2009/057554号公報International Publication No. 2009/057554 国際公開第2009/116635号公報International Publication No. 2009/116635

J. R. Wagner、J. Agric. Food. Chem.、2000年、48、p.3159−3165J. R. Wagner, J. Agric. Food. Chem., 2000, 48, p. 3159-3165

大豆たんぱく質の上記の問題は、特に、流動食等の乳化組成物に用いようとする際に顕著となる。
そこで、本発明は、分散性及び乳化性を向上させた、食品組成物用の大豆たんぱく質を提供することを目的とする。
The above-mentioned problem of soybean protein becomes remarkable especially when it is intended to be used in an emulsified composition such as a liquid diet.
Therefore, an object of the present invention is to provide a soybean protein for a food composition having improved dispersibility and emulsification.

上記課題に鑑み、鋭意研究した結果、本発明者らは、粉末状大豆たんぱく質のpHを調整し、加温・せん断の処理を行うことにより、分散性及び乳化性にすぐれた大豆たんぱく質が得られることを見出し、本発明を完成させた。
本発明によれば、以下の食品組成物用の大豆たんぱく質の製造方法等を提供できる。
1.食品組成物用の大豆たんぱく質の製造方法であって、次の各工程:
(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;
(b)前記分散液のpHを8〜12に調整する工程;
(c)前記分散液を加温しながらせん断する工程;及び
(d)前記分散液を中和する工程
を含み、
前記工程(b)と前記工程(c)のいずれを先に行ってもよい、前記製造方法。
2.前記工程(c)の加温の温度が20〜100℃である、1に記載の食品組成物用の大豆たんぱく質の製造方法。
3.前記工程(c)の後において、大豆たんぱく質の平均粒子径が500nm未満である、1又は2に記載の食品組成物用の大豆たんぱく質の製造方法。
4.前記工程(c)において、せん断応力1.3N/m以上で5分以上せん断を行う、1〜3のいずれかに記載の食品組成物用の大豆たんぱく質の製造方法。
5.前記粉末状大豆たんぱく質の10質量%水溶液のpHが6.8以上である、1〜4のいずれかに記載の食品組成物用の大豆たんぱく質の製造方法。
6.食品組成物の製造方法であって、次の各工程:
(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;
(b)前記分散液のpHを8〜12に調整する工程;
(c)前記分散液を加温しながらせん断する工程;
(d)前記分散液を中和する工程;
(e)前記分散液に、脂質、糖質、及びミネラルを加え、均質化して、食品組成物を得る工程
を含み、
前記工程(b)と前記工程(c)のいずれを先に行ってもよい、前記製造方法。
7.前記食品組成物が、前記食品組成物の全質量に対して0.1質量%以上の量の大豆たんぱく質を含む、6に記載の食品組成物の製造方法。
8.前記工程(c)の加温の温度が20〜100℃である、6又は7に記載の食品組成物の製造方法。
9.前記工程(c)の後において、大豆たんぱく質の平均粒子径が500nm未満である、6〜8のいずれかに記載の食品組成物の製造方法。
10.前記工程(c)において、せん断応力1.3N/m以上で5分以上せん断を行う、6〜9のいずれかに記載の食品組成物の製造方法。
11.前記粉末状大豆たんぱく質の10質量%水溶液のpHが6.8以上である、6〜10のいずれかに記載の食品組成物の製造方法。
In view of the above problems, as a result of diligent research, the present inventors can obtain soy protein having excellent dispersibility and emulsifying property by adjusting the pH of the powdered soy protein and performing the heating / shearing treatment. We found that and completed the present invention.
According to the present invention, it is possible to provide a method for producing soybean protein for the following food compositions.
1. 1. A method for producing soybean protein for food compositions, in which the following steps:
(A) Step of preparing a dispersion liquid in which powdered soybean protein is dispersed in water;
(B) Step of adjusting the pH of the dispersion to 8-12;
(C) A step of shearing the dispersion while heating; and (d) a step of neutralizing the dispersion.
The manufacturing method, wherein either the step (b) or the step (c) may be performed first.
2. The method for producing a soybean protein for a food composition according to 1, wherein the heating temperature in the step (c) is 20 to 100 ° C.
3. 3. The method for producing soybean protein for a food composition according to 1 or 2, wherein after the step (c), the average particle size of the soybean protein is less than 500 nm.
4. The method for producing soybean protein for a food composition according to any one of 1 to 3, wherein in the step (c), shearing is performed at a shear stress of 1.3 N / m 2 or more for 5 minutes or more.
5. The method for producing soybean protein for a food composition according to any one of 1 to 4, wherein the pH of the 10% by mass aqueous solution of the powdered soybean protein is 6.8 or more.
6. A method for producing a food composition, wherein each of the following steps:
(A) Step of preparing a dispersion liquid in which powdered soybean protein is dispersed in water;
(B) Step of adjusting the pH of the dispersion to 8-12;
(C) A step of shearing the dispersion while heating it;
(D) Step of neutralizing the dispersion liquid;
(E) The step of adding lipids, sugars and minerals to the dispersion and homogenizing the dispersion to obtain a food composition is included.
The manufacturing method, wherein either the step (b) or the step (c) may be performed first.
7. The method for producing a food composition according to 6, wherein the food composition contains 0.1% by mass or more of soybean protein with respect to the total mass of the food composition.
8. The method for producing a food composition according to 6 or 7, wherein the heating temperature in the step (c) is 20 to 100 ° C.
9. The method for producing a food composition according to any one of 6 to 8, wherein after the step (c), the average particle size of the soybean protein is less than 500 nm.
10. The method for producing a food composition according to any one of 6 to 9, wherein in the step (c), shearing is performed at a shear stress of 1.3 N / m 2 or more for 5 minutes or more.
11. The method for producing a food composition according to any one of 6 to 10, wherein the pH of the 10% by mass aqueous solution of the powdered soybean protein is 6.8 or more.

本発明によれば、分散性及び乳化性を向上させた、食品組成物用の大豆たんぱく質を提供することができる。 According to the present invention, it is possible to provide a soybean protein for a food composition having improved dispersibility and emulsification.

図1は、実験例3における沈殿率の結果を示す図である。FIG. 1 is a diagram showing the results of the precipitation rate in Experimental Example 3. 図2は、実験例3における脂肪球球径の結果を示す図である。FIG. 2 is a diagram showing the results of the fat bulb diameter in Experimental Example 3. 図3は、実験例3における粘度の結果を示す図である。FIG. 3 is a diagram showing the results of viscosity in Experimental Example 3. 図4は、実験例4における沈殿率の結果を示す図である。FIG. 4 is a diagram showing the results of the precipitation rate in Experimental Example 4. 図5は、実験例4における脂肪球球径の結果を示す図である。FIG. 5 is a diagram showing the results of the fat bulb diameter in Experimental Example 4. 図6は、実験例4における粘度の結果を示す図である。FIG. 6 is a diagram showing the results of viscosity in Experimental Example 4. 図7は、実験例4における耐熱性の結果を示す図である。FIG. 7 is a diagram showing the results of heat resistance in Experimental Example 4.

以下、本発明の食品組成物用の大豆たんぱく質の製造方法、及び食品組成物の製造方法について説明する。
本明細書中において、「食品組成物」は医薬用途ではないものとする。したがって、本明細書中において、「食品組成物」は、「医薬品」、「医薬品の流動食」等は含まない。
Hereinafter, a method for producing a soybean protein for a food composition of the present invention and a method for producing a food composition will be described.
In the present specification, "food composition" shall not be used for pharmaceutical purposes. Therefore, in the present specification, "food composition" does not include "pharmaceutical products", "liquid foods of pharmaceutical products" and the like.

[食品組成物用の大豆たんぱく質の製造方法]
本発明の食品組成物用の大豆たんぱく質の製造方法は、次の各工程:(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;(b)前記分散液のpHを10〜12に調整する工程;(c)前記分散液を加温しながらせん断する工程;及び(d)前記分散液を中和する工程を含むものである。本発明の製造法においては、前記工程(b)と前記工程(c)のいずれを先に行ってもよい。
[Manufacturing method of soy protein for food composition]
The method for producing a soybean protein for a food composition of the present invention includes the following steps: (a) a step of preparing a dispersion in which powdered soybean protein is dispersed in water; (b) a pH of the dispersion is 10 It includes a step of adjusting to -12; (c) a step of shearing the dispersion while heating; and (d) a step of neutralizing the dispersion. In the production method of the present invention, either the step (b) or the step (c) may be performed first.

本発明の製造方法にしたがえば、分散性及び乳化性にすぐれた大豆たんぱく質を製造することができる。また、本発明の製造方法により製造される大豆たんぱく質は、食品組成物の材料として使用した場合に、乳化性にすぐれ、大豆たんぱく質の沈殿・凝集が少なく分散性にすぐれ、粘度が低く、耐熱性にすぐれた食品組成物を提供できる。 According to the production method of the present invention, soybean protein having excellent dispersibility and emulsifying property can be produced. Further, the soybean protein produced by the production method of the present invention has excellent emulsifying property, less precipitation / aggregation of soybean protein, excellent dispersibility, low viscosity, and heat resistance when used as a material for food compositions. Can provide excellent food compositions.

工程(a):分散液調製工程
本発明の食品組成物用の大豆たんぱく質の製造方法では、工程(a)として、粉末状大豆たんぱく質を水に分散させた分散液を調製する(分散液調製工程(a))。
原料として使用する粉末状大豆たんぱく質は、特に制限されず、一般的に入手可能なものを使用できる。市販されている商品としては、例えば、ソルピー4000H(日清オイリオ社製)、プロファム649(ADM社製)、プロファム974(ADM社製)、プロファム781(ADM社製)、プロファム825(ADM社製)、XT219D(solae社製)、710IP(solae社製)等が挙げられる。
Step (a): Dispersion solution preparation step In the method for producing soybean protein for a food composition of the present invention, as step (a), a dispersion solution in which powdered soybean protein is dispersed in water is prepared (dispersion solution preparation step). (A)).
The powdered soybean protein used as a raw material is not particularly limited, and generally available ones can be used. Examples of commercially available products include Solpy 4000H (manufactured by Nisshin Oillio), Profam 649 (manufactured by ADM), Profam 974 (manufactured by ADM), Profam 781 (manufactured by ADM), and Profam 825 (manufactured by ADM). ), XT219D (manufactured by solo), 710IP (manufactured by solo) and the like.

水は、食品用途に使用可能であることを条件として特に制限はなく、水道水、蒸留水、イオン交換水等を使用できる。 The water is not particularly limited as long as it can be used for food purposes, and tap water, distilled water, ion-exchanged water and the like can be used.

粉末状大豆たんぱく質を水に分散させる手段は、特に制限されず、当技術分野において既知の任意の方法を使用できる。 The means for dispersing the powdered soybean protein in water is not particularly limited, and any method known in the art can be used.

分散液中の粉末状大豆たんぱく質の濃度は、特に制限されないが、例えば、0.5〜10質量%であり、好ましくは1〜7質量%である。 The concentration of powdered soybean protein in the dispersion is not particularly limited, but is, for example, 0.5 to 10% by mass, preferably 1 to 7% by mass.

粉末状大豆たんぱく質は、10質量%水溶液のpHが6.8以上であることが好ましい。
粉末状大豆たんぱく質は、5質量%水溶液の粘度が5mPa・s以上であることが好ましく、10mPa・s以上であることがより好ましい。5質量%水溶液の粘度が5mPa・s以上である場合に本発明の効果がより発揮され、本発明の製造方法により製造された大豆たんぱく質を用いて得られる食品組成物は、乳化性にすぐれ、沈殿・凝集が少なく分散性にすぐれ、粘度が低く、耐熱性にすぐれたものとすることができる。
The pH of the 10% by mass aqueous solution of the powdered soybean protein is preferably 6.8 or more.
The viscosity of the 5% by mass aqueous solution of the powdered soybean protein is preferably 5 mPa · s or more, and more preferably 10 mPa · s or more. The effect of the present invention is more exerted when the viscosity of the 5% by mass aqueous solution is 5 mPa · s or more, and the food composition obtained by using the soy protein produced by the production method of the present invention has excellent emulsifying property. It can be made to have little precipitation / aggregation, excellent dispersibility, low viscosity, and excellent heat resistance.

工程(b):pH調整工程
本発明の食品組成物用の大豆たんぱく質の製造方法では、工程(b)として、分散液のpHを8〜12、好ましくは10〜12に調整する(pH調製工程(b))。工程(b)は、前述の工程(a)の後に行うが、後述する工程(c)より先に行ってもよく、又は、後述する工程(c)の後に行ってもよい。仮に乳化安定性の良好な大豆たんぱく質があった場合に、分散液のpH調整条件を適宜変更でき、例えば、分散液のpHを8〜12、9〜12、8〜11、9〜11、8〜10、9〜10、8〜9に調整することができることは言うまでもない。
Step (b): pH adjustment step In the method for producing soy protein for a food composition of the present invention, the pH of the dispersion is adjusted to 8 to 12, preferably 10 to 12 as step (b) (pH adjustment step). (B)). The step (b) is performed after the above-mentioned step (a), but may be performed before the step (c) described later, or may be performed after the step (c) described later. If there is a soybean protein with good emulsion stability, the pH adjustment conditions of the dispersion can be changed as appropriate. For example, the pH of the dispersion can be changed to 8-12, 9-12, 8-11, 9-11, 8 Needless to say, it can be adjusted to 10, 9 to 10, 8 to 9.

pHの調整は、水酸化ナトリウム水溶液等の任意の塩基を用いて行うことができる。 The pH can be adjusted using any base such as an aqueous sodium hydroxide solution.

工程(c):加温せん断工程
本発明の食品組成物用の大豆たんぱく質の製造方法では、工程(c)として、分散液を加温しながらせん断する(加温せん断工程(c))。工程(c)は、前述の工程(a)の後に行うが、前述の工程(b)より先に行ってもよく、又は、前述の工程(b)の後に行ってもよい。
Step (c): Warming shearing step In the method for producing soybean protein for food compositions of the present invention, as step (c), the dispersion is sheared while being heated (warming shearing step (c)). The step (c) is performed after the above-mentioned step (a), but may be performed before the above-mentioned step (b) or after the above-mentioned step (b).

本明細書中において、加温は、加熱することにより加熱前よりも高い温度にすることを意味する。加温の温度は、好ましくは20〜100℃であり、より好ましくは50〜85℃であり、さらにより好ましくは60〜70℃である。 In the present specification, heating means to raise the temperature by heating to a temperature higher than that before heating. The heating temperature is preferably 20 to 100 ° C, more preferably 50 to 85 ° C, and even more preferably 60 to 70 ° C.

工程(c)の後において、大豆たんぱく質の平均粒子径が500nm未満であることが好ましく、400nm未満であることがより好ましい。大豆たんぱく質の平均粒子径を500nm未満とすることにより、分散性と乳化性をより向上させることができる。大豆たんぱく質の平均粒子径は、動的光散乱法式粒子径測定装置(ゼータサイザーナノ、スペクトリス社製)を用いて測定される平均粒子径(z−average(d.nm))を採用する。 After the step (c), the average particle size of the soybean protein is preferably less than 500 nm, more preferably less than 400 nm. By setting the average particle size of the soybean protein to less than 500 nm, the dispersibility and emulsifying property can be further improved. For the average particle size of the soybean protein, an average particle size (z-avarage (d. Nm)) measured using a dynamic light scattering method particle size measuring device (Zetasizer Nano, manufactured by Spectris) is adopted.

工程(c)において、せん断は、既知の手段を用いて行うことができる。せん断の条件は、用いる手段に依存して、適宜決定することができる。例えば、せん断は、せん断応力1.3N/m以上で5分以上行うことが好ましい。加温下で、かつ、このような条件でせん断を行うことにより、大豆たんぱく質の平均粒子径を小さくすることができ(例えば、500nm未満)、分散性と乳化性を向上させることができる。 In step (c), shearing can be performed using known means. The shearing conditions can be appropriately determined depending on the means used. For example, shearing is preferably performed at a shear stress of 1.3 N / m 2 or more for 5 minutes or more. By performing shearing under such conditions under heating, the average particle size of soybean protein can be reduced (for example, less than 500 nm), and dispersibility and emulsification can be improved.

前述の工程(b)と工程(c)は、工程(b)を先に行い、その後に工程(c)を行うことが好ましい。pHが高い状態で、加温しながらせん断を行うことで、本発明の効果をより発揮することができる。 In the above-mentioned steps (b) and (c), it is preferable that the step (b) is performed first and then the step (c) is performed. The effect of the present invention can be more exerted by performing shearing while heating in a high pH state.

工程(d):中和工程
本発明の食品組成物用の大豆たんぱく質の製造方法では、工程(d)として、分散液を中和する(中和工程(d))。中和することにより、得られた大豆たんぱく質をそのまま使用して食品組成物を製造するために使用できる。
中和は、任意の酸を用いて行うことができる。
中和する際の温度は特に限定されないが、例えば、室温、20℃等である。
Step (d): Neutralization step In the method for producing soy protein for a food composition of the present invention, the dispersion is neutralized as step (d) (neutralization step (d)). By neutralizing, the obtained soybean protein can be used as it is for producing a food composition.
Neutralization can be carried out with any acid.
The temperature at the time of neutralization is not particularly limited, but is, for example, room temperature, 20 ° C., or the like.

[食品組成物の製造方法]
本発明の食品組成物の製造方法は、次の各工程:(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;(b)前記分散液のpHを10〜12に調整する工程;(c)前記分散液を加温しながらせん断する工程;(d)前記分散液を中和する工程;(e)前記分散液に、脂質、糖質、及びミネラルを加え、均質化して、食品組成物を得る工程を含むものである。本発明の製造法においては、前記工程(b)と前記工程(c)のいずれを先に行ってもよい。
本発明の製造方法にしたがえば、乳化性にすぐれ、大豆たんぱく質の沈殿・凝集が少なく分散性にすぐれ、粘度が低く、耐熱性にすぐれた食品組成物を製造することができる。
[Manufacturing method of food composition]
The method for producing a food composition of the present invention includes the following steps: (a) a step of preparing a dispersion in which powdered soybean protein is dispersed in water; (b) adjusting the pH of the dispersion to 10 to 12. Steps; (c) Step of shearing the dispersion while heating; (d) Step of neutralizing the dispersion; (e) Add lipids, sugars and minerals to the dispersion to homogenize. It includes a step of obtaining a food composition. In the production method of the present invention, either the step (b) or the step (c) may be performed first.
According to the production method of the present invention, it is possible to produce a food composition having excellent emulsifying property, less precipitation / aggregation of soy protein, excellent dispersibility, low viscosity, and excellent heat resistance.

本明細書中において、「食品組成物」とは、例えば、流動食、栄養食品、飲料等である。 In the present specification, the "food composition" is, for example, a liquid food, a nutritional food, a beverage, or the like.

工程(a):分散液調製工程
本発明の食品組成物の製造方法では、工程(a)として、粉末状大豆たんぱく質を水に分散させた分散液を調製する(分散液調製工程(a))。工程(a)は、前述の本発明の食品組成物用の大豆たんぱく質の製造方法における工程(a)と同様に行うことができる。
Step (a): Dispersion liquid preparation step In the method for producing a food composition of the present invention, as step (a), a dispersion liquid in which powdered soybean protein is dispersed in water is prepared (dispersion liquid preparation step (a)). .. The step (a) can be carried out in the same manner as the step (a) in the above-mentioned method for producing a soybean protein for a food composition of the present invention.

工程(b):pH調整工程
本発明の食品組成物の製造方法では、工程(b)として、分散液のpHを10〜12に調整する(pH調製工程(b))。工程(b)は、前述の工程(a)の後に行うが、後述する工程(c)より先に行ってもよく、又は、後述する工程(c)の後に行ってもよい。工程(b)は、前述の本発明の食品組成物用の大豆たんぱく質の製造方法における工程(b)と同様に行うことができる。
Step (b): pH adjustment step In the method for producing a food composition of the present invention, the pH of the dispersion is adjusted to 10 to 12 as step (b) (pH adjustment step (b)). The step (b) is performed after the above-mentioned step (a), but may be performed before the step (c) described later, or may be performed after the step (c) described later. The step (b) can be carried out in the same manner as the step (b) in the above-mentioned method for producing a soybean protein for a food composition of the present invention.

工程(c):加温せん断工程
本発明の食品組成物の製造方法では、工程(c)として、分散液を加温しながらせん断する(加温せん断工程(c))。工程(c)は、前述の工程(a)の後に行うが、前述の工程(b)より先に行ってもよく、又は、前述の工程(b)の後に行ってもよい。工程(c)は、前述の本発明の食品組成物用の大豆たんぱく質の製造方法における工程(c)と同様に行うことができる。
Step (c): Warming Shear Step In the method for producing a food composition of the present invention, as a step (c), the dispersion liquid is sheared while being heated (warming shear step (c)). The step (c) is performed after the above-mentioned step (a), but may be performed before the above-mentioned step (b) or after the above-mentioned step (b). The step (c) can be carried out in the same manner as the step (c) in the above-mentioned method for producing a soybean protein for a food composition of the present invention.

前述の工程(b)と工程(c)は、工程(b)を先に行い、その後に工程(c)を行うことが好ましい。pHが高い状態で、加温しながらせん断を行うことで、本発明の効果をより発揮することができる。 In the above-mentioned steps (b) and (c), it is preferable that the step (b) is performed first and then the step (c) is performed. The effect of the present invention can be more exerted by performing shearing while heating in a high pH state.

工程(d):中和工程
本発明の食品組成物の製造方法では、工程(d)として、分散液を中和する(中和工程(d))。工程(d)は、前述の本発明の食品組成物用の大豆たんぱく質の製造方法における工程(d)と同様に行うことができる。
Step (d): Neutralization step In the method for producing a food composition of the present invention, the dispersion is neutralized as step (d) (neutralization step (d)). The step (d) can be carried out in the same manner as the step (d) in the above-mentioned method for producing a soybean protein for a food composition of the present invention.

工程(e):均質化工程
本発明の食品組成物の製造方法では、工程(e)として、分散液に、脂質、糖質、及びミネラルを加え、均質化して、食品組成物を得る(均質化工程(e))。
Step (e): Homogenization step In the method for producing a food composition of the present invention, as step (e), lipids, sugars and minerals are added to the dispersion and homogenized to obtain a food composition (homogeneity). Chemical step (e)).

脂質、糖質、及びミネラルは、それぞれ特に制限されず、食品用途に通常使用される材料を適宜使用できる。また、その他の食品材料、添加剤等を必要に応じて使用してもよい。 The lipids, sugars, and minerals are not particularly limited, and materials usually used for food applications can be appropriately used. In addition, other food materials, additives and the like may be used as needed.

均質化は、当技術分野において既知の任意の方法を使用して行うことができる。 Homogeneity can be performed using any method known in the art.

本発明の製造方法により製造される食品組成物は、食品組成物の全質量に対して0.1質量%以上の量の大豆たんぱく質を含むことが好ましい。 The food composition produced by the production method of the present invention preferably contains 0.1% by mass or more of soybean protein with respect to the total mass of the food composition.

以下、実施例を示して本発明をさらに具体的に説明するが、本発明の範囲はこれら実施例の記載に何ら限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to Examples, but the scope of the present invention is not limited to the description of these Examples.

実施例における各パラメータの測定手順は以下のとおりである。
[沈殿量及び沈殿率]
試料25mLを遠沈管に採取し、1,400Gで1時間遠心した後、得られた沈殿物を60℃の乾燥機にて水分が完全に蒸発するまで乾燥させ、測定した重量を沈殿量とした。また、測定した沈殿量を、試料25mLに添加されている粉末状大豆たんぱく質の総重量で除し、百分率で表した値を沈殿率とした。沈殿率は、試料となる食品などの設計条件によるものであるが、値が小さいほど好ましく、例えば、20%以下が好ましく、15%以下がより好ましく、12%以下がさらに好ましく、10%以下が特に好ましい。
The measurement procedure of each parameter in the embodiment is as follows.
[Precipitation amount and precipitation rate]
25 mL of the sample was collected in a centrifuge tube, centrifuged at 1,400 G for 1 hour, and then the obtained precipitate was dried in a dryer at 60 ° C. until the water was completely evaporated, and the measured weight was taken as the amount of precipitate. .. Further, the measured amount of precipitation was divided by the total weight of powdered soybean protein added to 25 mL of the sample, and the value expressed as a percentage was taken as the precipitation rate. The precipitation rate depends on the design conditions of the food to be sample, but the smaller the value, the more preferable, for example, 20% or less is preferable, 15% or less is more preferable, 12% or less is further preferable, and 10% or less is preferable. Especially preferable.

[pH]
pHメーター(F−52型(HORIBA社製))を用いて、試料のpHを測定した。
[PH]
The pH of the sample was measured using a pH meter (F-52 type (manufactured by HORIBA)).

[粘度]
20℃、せん断速度100s−1における試料の粘度を、共軸二重円筒形回転粘度計(RheolabQC、Antrn Paar社製)によって測定した。
[viscosity]
The viscosity of the sample at 20 ° C. and a shear rate of 100 s- 1 was measured with a co-axial double cylindrical rotational viscometer (RheolabQC, manufactured by Antrn Par).

[解乳化率]
試料10mLを遠沈管に採取し、95℃で20分間加熱した後、1,400Gで1時間遠心して分離した油層の体積を測定した。この分離した油層の体積を、乳化組成物10mLに添加されている油脂の総体積で除し、百分率で表した値を解乳化率とした。
[Emulsification rate]
10 mL of the sample was collected in a centrifuge tube, heated at 95 ° C. for 20 minutes, and then centrifuged at 1,400 G for 1 hour to measure the volume of the separated oil layer. The volume of the separated oil layer was divided by the total volume of the fats and oils added to 10 mL of the emulsification composition, and the value expressed as a percentage was taken as the emulsification rate.

[脂肪球球径]
試料の20℃における平均粒子径について、動的光散乱法式粒子径測定装置(ゼータサイザーナノ、スペクトリス社製)を用いて測定した。
[Fat bulb diameter]
The average particle size of the sample at 20 ° C. was measured using a dynamic light scattering method particle size measuring device (Zetasizer Nano, manufactured by Spectris).

[耐熱性試験]
レトルト殺菌する前の試料を採取し、水酸化ナトリウムを用いてpHを6.8(未調整)、7.0、7.2に調整した。これらをガラス製バイアルに各3mLずつ入れ密栓し、約3cm幅で毎分約200回振とうしつつ130℃で加熱し続けた際、凝集物が目視にて確認できるようになった時間を測定した。
[Heat resistance test]
Samples before retort sterilization were taken and the pH was adjusted to 6.8 (unadjusted), 7.0 and 7.2 with sodium hydroxide. When 3 mL each of these was placed in a glass vial, sealed, and continuously heated at 130 ° C. with a width of about 3 cm and shaken about 200 times per minute, the time during which the agglomerates became visible was measured. did.

実験例1
粉末状大豆たんぱく質(プロファム649:ADM社製)を水に分散させて5質量%の分散液を調整し、水酸化ナトリウム水溶液を用いてpH=7、8、9、10、11、12の各試料を調製した。それぞれの試料について、60℃になるよう加熱して、温度を維持したまま、ホモミキサー(本体:T25 digital ULTRA−TURRAX(登録商標)、ジェネレーター:S25N−8G、ともにIKA社製)を用いて20,000rpmで5分間せん断し、クエン酸を用いて中和して、分散液の各pH毎の、沈殿率を比較した。結果を表1に示す。
Experimental Example 1
Powdered soy protein (Profem 649: manufactured by ADM) was dispersed in water to prepare a 5% by mass dispersion, and pH = 7, 8, 9, 10, 11 and 12 were prepared using an aqueous sodium hydroxide solution. A sample was prepared. Each sample was heated to 60 ° C., and while maintaining the temperature, 20 using a homomixer (main body: T25 digital ULTRA-TURRAX (registered trademark), generator: S25N-8G, both manufactured by IKA). Shearing at 000 rpm for 5 minutes and neutralizing with citric acid, the precipitation rates of the dispersions at each pH were compared. The results are shown in Table 1.

Figure 0006771335
Figure 0006771335

加温・せん断を行う際のpHを高くするほど、沈殿率は低くなり、大豆たんぱく質の凝集が少なく沈殿が少なくなる結果が得られた。特にpH10〜12では、大豆たんぱく質の沈殿は問題とならないほど沈殿率が低くなり、沈殿率の値はほぼ変わらない結果が得られた。 The higher the pH at the time of heating and shearing, the lower the precipitation rate, and the result was that soybean protein aggregated less and precipitation decreased. In particular, at pHs 10 to 12, the precipitation rate of soybean protein was so low that it did not matter, and the results showed that the precipitation rate values were almost unchanged.

実験例2
粉末状大豆たんぱく質(プロファム649:ADM社製)を水に分散させて5質量%の分散液を調製し、水酸化ナトリウム水溶液を用いてpH=7、10、12の各試料を調製した。それぞれの試料について、60℃になるよう加熱して、温度を維持したまま、ホモミキサー(本体:T25 digital ULTRA−TURRAX(登録商標)、ジェネレーター:S25N−8G、ともにIKA社製)を用いて20,000rpmで5分間せん断し、クエン酸を用いて中和した。
Experimental Example 2
Powdered soybean protein (Profemme 649: manufactured by ADM) was dispersed in water to prepare a 5% by mass dispersion, and samples having pH = 7, 10 and 12 were prepared using an aqueous sodium hydroxide solution. Each sample was heated to 60 ° C., and while maintaining the temperature, 20 using a homomixer (main body: T25 digital ULTRA-TURRAX (registered trademark), generator: S25N-8G, both manufactured by IKA). Sheared at 000 rpm for 5 minutes and neutralized with citric acid.

中和後のたんぱく質分散液について、全量が30mL、たんぱく質濃度が5質量%、0.25質量%となるように水で希釈してから、油脂20mLを加えて、撹拌しながら60℃まで加温し、温度を維持しながら、ホモミキサー(本体:T25 digital ULTRA−TURRAX(登録商標)、ジェネレーター:S25N−8G、ともにIKA社製)を用いて20,000rpmで3分間乳化させて、乳化食品組成物を得た。得られた乳化油脂組成物中のたんぱく質濃度は、それぞれ、3質量%、0.15質量%である。 Dilute the neutralized protein dispersion with water so that the total volume is 30 mL and the protein concentration is 5% by mass and 0.25% by mass, then add 20 mL of fat and oil and heat to 60 ° C with stirring. Then, while maintaining the temperature, emulsify using a homomixer (main body: T25 digital ULTRA-TURRAX (registered trademark), generator: S25N-8G, both manufactured by IKA) at 20,000 rpm for 3 minutes to compose the emulsified food. I got something. The protein concentrations in the obtained emulsified oil / fat composition are 3% by mass and 0.15% by mass, respectively.

たんぱく質濃度が3質量%の乳化食品組成物について、粘度、沈殿率を測定し、たんぱく質濃度が0.15質量%の乳化食品組成物について、解乳化率を測定した。結果を表2に示す。 The viscosity and precipitation rate of the emulsified food composition having a protein concentration of 3% by mass were measured, and the demulsification rate was measured for the emulsified food composition having a protein concentration of 0.15% by mass. The results are shown in Table 2.

Figure 0006771335
Figure 0006771335

pH10、12で加温・せん断処理を行って得られた大豆たんぱく質を使用した場合、pH7で加温・せん断処理を行って得られた大豆たんぱく質を使用した場合と比較して、粘度、沈殿率、解乳化率ともに低い乳化食品組成物が得られた。 When soy protein obtained by heating / shearing at pH 10 or 12 is used, the viscosity and precipitation rate are higher than those obtained by using soy protein obtained by heating / shearing at pH 7. , An emulsified food composition having a low emulsification rate was obtained.

実験例3
試料のpHを10に調整し、加温・せん断処理の温度とせん断条件を変更したことを除いては、実験例2と同様にして、乳化食品組成物を調製した。加温・せん断処理の温度は20℃(加温せず)、60℃(加温)、せん断条件は、回転数を0rpm(せん断せず)、10,000rpm、20,000rpmとした。得られた乳化油脂組成物中のたんぱく質濃度は、それぞれ、3質量%、0.15質量%である。
たんぱく質濃度が3質量%の乳化食品組成物について、粘度、沈殿率を測定し、たんぱく質濃度が0.15質量%の乳化食品組成物について、脂肪球球径を測定した。結果を図1〜3に示す。
Experimental Example 3
An emulsified food composition was prepared in the same manner as in Experimental Example 2 except that the pH of the sample was adjusted to 10 and the heating / shearing temperature and shearing conditions were changed. The temperature of the heating / shearing treatment was 20 ° C. (without heating) and 60 ° C. (heating), and the rotation speed was 0 rpm (without shearing), 10,000 rpm and 20,000 rpm. The protein concentrations in the obtained emulsified oil / fat composition are 3% by mass and 0.15% by mass, respectively.
The viscosity and precipitation rate were measured for the emulsified food composition having a protein concentration of 3% by mass, and the fat bulb diameter was measured for the emulsified food composition having a protein concentration of 0.15% by mass. The results are shown in FIGS.

温度が高いほど、また、せん断速度が高いほど、沈殿率、粘度が低く、脂肪球球径が小さい(乳化性が高い)結果が得られた。 The higher the temperature and the higher the shear rate, the lower the precipitation rate and viscosity, and the smaller the fat bulb diameter (higher emulsifying property).

実験例6
たんぱく質配合比として、粉末状大豆たんぱく質を100%使用し、表3に示す配合で流動食A〜Cを調製した。具体的な調製手順を以下に説明する。
Experimental Example 6
As a protein blending ratio, 100% powdered soybean protein was used, and liquid foods A to C were prepared according to the blending shown in Table 3. The specific preparation procedure will be described below.

(流動食A)
水に粉末状大豆たんぱく質を分散させた後、ナトリウム及びカリウムとして炭酸ナトリウムと炭酸カリウムを加えてpHを約10に調整後、60℃に加熱し、ホモミキサー(本体:ROBOMICS(特殊機化工業社製)、ジェネレーター:ホモミクサーマークII)を用いて12,000rpmで10分間高速せん断を行い、次いでクエン酸にて中和した。
これに炭水化物、カルシウム、マグネシウムを添加して、混合し、次いで、脂質を予備分散させ、高圧ホモジナイザーを用いて35MPaで均質化を行い、pHを約6.8に調整した後、100重量部になるように補水した。次いで、250mL缶に充填して密封し、121℃で20分間レトルト殺菌を行い、流動食Aを得た。
(Liquid food A)
After dispersing powdered soybean protein in water, add sodium carbonate and potassium carbonate as sodium and potassium to adjust the pH to about 10, and then heat to 60 ° C. Homomixer (main body: ROBOMICS (Special Machinery Chemical Industry Co., Ltd.) , Generator: Homomixer Mark II) was used for high-speed shearing at 12,000 rpm for 10 minutes, and then neutralized with citric acid.
Carbohydrates, calcium and magnesium are added to this and mixed, then lipids are pre-dispersed, homogenized at 35 MPa using a high-pressure homogenizer, the pH is adjusted to about 6.8, and then to 100 parts by weight. Water was replenished so as to become. Then, the 250 mL can was filled and sealed, and retort sterilized at 121 ° C. for 20 minutes to obtain liquid food A.

(流動食B)
pHを約12に調整して加温・せん断の処理を行ったことを除いては、栄養剤Aと同様の手順にしたがい、表3に示す配合で流動食Bを調製した。
(Liquid food B)
Liquid food B was prepared according to the same procedure as that for nutritional supplement A, except that the pH was adjusted to about 12 and the heating / shearing treatment was performed.

(流動食C)
水に粉末状大豆たんぱく質を分散させた後、炭水化物、ナトリウム、カリウム、カルシウム、マグネシウムを添加して、混合し、次いで、脂質を予備分散させ、高圧ホモジナイザーを用いて35MPaで均質化を行い、pHを約6.8に調整した後、100重量部になるように補水した。次いで、250mL缶に充填して密封し、121℃で20分間レトルト殺菌を行い、流動食Cを得た。
(Liquid food C)
After dispersing powdered soy protein in water, carbohydrates, sodium, potassium, calcium and magnesium are added and mixed, then the lipids are pre-dispersed and homogenized at 35 MPa using a high-pressure homogenizer to perform pH. Was adjusted to about 6.8, and then water was replenished to 100 parts by weight. Next, the 250 mL can was filled and sealed, and retort sterilized at 121 ° C. for 20 minutes to obtain a liquid food C.

Figure 0006771335
Figure 0006771335

得られた流動食A〜Cについて、粘度、沈殿量、脂肪球球径、耐熱性を評価した。結果を図2〜5に示す。流動食C(未処理)と、流動食A、Bを比較すると、粘度、沈殿量がともに低下し、脂肪球球径も小さくなっていることが確認された。また、耐熱性も向上していることが確認された。 The obtained liquid foods A to C were evaluated for viscosity, precipitation amount, fat bulb diameter, and heat resistance. The results are shown in Figures 2-5. Comparing the liquid food C (untreated) with the liquid foods A and B, it was confirmed that both the viscosity and the amount of precipitation decreased, and the diameter of the fat bulb was also reduced. It was also confirmed that the heat resistance was also improved.

本発明により製造される大豆たんぱく質を用いることにより、乳化性にすぐれ、沈殿・凝集が少なく分散性にすぐれ、粘度が低く、耐熱性にすぐれた食品組成物を、従来の製造設備を利用して簡便に製造することができる。
By using the soy protein produced by the present invention, a food composition having excellent emulsifying property, less precipitation / aggregation, excellent dispersibility, low viscosity, and excellent heat resistance can be produced by using a conventional production facility. It can be easily manufactured.

Claims (12)

流動食用の大豆たんぱく質の製造方法であって、次の各工程:
(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;
(b)前記分散液のpHを8〜12に調整する工程;
(c)前記分散液を加温しながらせん断する工程;及び
(d)前記分散液を中和する工程
を含み、
前記工程(b)と前記工程(c)のいずれを先に行ってもよく、
前記工程(c)の後において、大豆たんぱく質の平均粒子径が500nm未満である、前記製造方法。
A method of manufacturing a soy protein for liquid food, the following steps:
(A) Step of preparing a dispersion liquid in which powdered soybean protein is dispersed in water;
(B) Step of adjusting the pH of the dispersion to 8-12;
(C) A step of shearing the dispersion while heating; and (d) a step of neutralizing the dispersion.
Rather it may also be carried out either in the step (b) and the step of (c) above,
The production method, wherein the average particle size of the soybean protein is less than 500 nm after the step (c) .
前記工程(c)の加温の温度が20〜100℃である、請求項1に記載の流動食用の大豆たんぱく質の製造方法。 The temperature of the heating step (c) is 20 to 100 ° C., the production method of soybean protein for liquid diet according to claim 1. 前記工程(c)の加温の温度が50〜85℃である、請求項1又は2に記載の流動食用の大豆たんぱく質の製造方法。The method for producing a liquid edible soybean protein according to claim 1 or 2, wherein the heating temperature in the step (c) is 50 to 85 ° C. 前記工程(c)において、せん断応力1.3N/m以上で5分以上せん断を行う、請求項1〜3のいずれかに記載の流動食用の大豆たんぱく質の製造方法。 Wherein In the step (c), the performing shearing 5 minutes or more at a shear stress 1.3 N / m 2 or more, the production method of soybean protein for liquid diet according to claim 1. 前記粉末状大豆たんぱく質の10質量%水溶液のpHが6.8以上である、請求項1〜4のいずれかに記載の流動食用の大豆たんぱく質の製造方法。 The pH of the powdered soybean 10% by weight aqueous solution of protein is 6.8 or more, the production method of soybean protein for liquid diet according to any one of claims 1 to 4. 流動食の製造方法であって、次の各工程:
(a)粉末状大豆たんぱく質を水に分散させた分散液を調製する工程;
(b)前記分散液のpHを8〜12に調整する工程;
(c)前記分散液を加温しながらせん断する工程;
(d)前記分散液を中和する工程;
(e)前記分散液に、脂質、糖質、及びミネラルを加え、均質化して、流動食を得る工程
を含み、
前記工程(b)と前記工程(c)のいずれを先に行ってもよく、
前記工程(c)の後において、大豆たんぱく質の平均粒子径が500nm未満である、前記製造方法。
A method for producing liquid food , and the following steps:
(A) Step of preparing a dispersion liquid in which powdered soybean protein is dispersed in water;
(B) Step of adjusting the pH of the dispersion to 8-12;
(C) A step of shearing the dispersion while heating it;
(D) Step of neutralizing the dispersion liquid;
(E) The step of adding lipids, sugars and minerals to the dispersion and homogenizing the dispersion to obtain a liquid food is included.
Rather it may also be carried out either in the step (b) and the step of (c) above,
The production method, wherein after the step (c), the average particle size of the soybean protein is less than 500 nm .
前記流動食が、前記流動食の全質量に対して0.1質量%以上の量の大豆たんぱく質を含む、請求項6に記載の流動食の製造方法。 The liquid diet is, the containing soybean protein in 0.1 mass% or more in an amount relative to the total weight of the liquid diet, method of manufacturing a liquid food according to claim 6. 前記工程(c)の加温の温度が20〜100℃である、請求項6又は7に記載の流動食の製造方法。 The method for producing a liquid food according to claim 6 or 7, wherein the heating temperature in the step (c) is 20 to 100 ° C. 前記工程(c)の加温の温度が50〜85℃である、請求項6〜8のいずれかに記載の流動食の製造方法。The method for producing a liquid food according to any one of claims 6 to 8, wherein the heating temperature in the step (c) is 50 to 85 ° C. 前記工程(c)において、せん断応力1.3N/m以上で5分以上せん断を行う、請求項6〜9のいずれかに記載の流動食の製造方法。 The method for producing a liquid food according to any one of claims 6 to 9, wherein in the step (c), shearing is performed at a shear stress of 1.3 N / m 2 or more for 5 minutes or more. 前記粉末状大豆たんぱく質の10質量%水溶液のpHが6.8以上である、請求項6〜10のいずれかに記載の流動食の製造方法。 The method for producing a liquid food according to any one of claims 6 to 10, wherein the pH of the 10% by mass aqueous solution of the powdered soybean protein is 6.8 or more. 前記工程(e)の後に、121℃で20分間レトルト殺菌を行う、請求項6〜11のいずれかに記載の流動食の製造方法。The method for producing a liquid food according to any one of claims 6 to 11, wherein the retort sterilization is performed at 121 ° C. for 20 minutes after the step (e).
JP2016161419A 2016-08-19 2016-08-19 Method for producing soy protein for food composition and method for producing food composition Active JP6771335B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2016161419A JP6771335B2 (en) 2016-08-19 2016-08-19 Method for producing soy protein for food composition and method for producing food composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016161419A JP6771335B2 (en) 2016-08-19 2016-08-19 Method for producing soy protein for food composition and method for producing food composition

Publications (2)

Publication Number Publication Date
JP2018027066A JP2018027066A (en) 2018-02-22
JP6771335B2 true JP6771335B2 (en) 2020-10-21

Family

ID=61248127

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016161419A Active JP6771335B2 (en) 2016-08-19 2016-08-19 Method for producing soy protein for food composition and method for producing food composition

Country Status (1)

Country Link
JP (1) JP6771335B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3967731A1 (en) * 2020-09-09 2022-03-16 Xampla Limited Protein dispersions

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NZ183822A (en) * 1976-05-03 1980-05-08 Itt Method for preparing a lipoprotein emulsion :an egg yolk replacer
US20140010940A1 (en) * 2012-06-25 2014-01-09 Brent E. Green Soy protein product with neutral or near neutral ph ("s701n2")
JP2014079241A (en) * 2012-09-28 2014-05-08 Showa Sangyo Co Ltd Processed soybean protein gel and processed soybean protein powder

Also Published As

Publication number Publication date
JP2018027066A (en) 2018-02-22

Similar Documents

Publication Publication Date Title
JP6648873B1 (en) Oil-fat emulsified composition containing protein for producing emulsified food
CN101959423B (en) Modification method of whey protein
Mantovani et al. Gelation of oil-in-water emulsions stabilized by whey protein
Liang et al. Effects of globular protein type and concentration on the physical properties and flow behaviors of oil-in-water emulsions stabilized by micellar casein–globular protein mixtures
JP7213189B2 (en) Method for producing water-soluble or water-dispersible fine particles, use or method of use as a substitute for emulsifying function, method for producing emulsion, method for producing food, and food containing emulsion
JPH09215480A (en) Mayonnaise-like products and their manufacturing method
JP5267465B2 (en) Concentrated liquid food using soy protein ingredients
WO2009154448A1 (en) Composition with fat gradient
Sun et al. Improving emulsifying properties using mixed natural emulsifiers: Tea saponin and golden pompano protein
JP2020521487A (en) Method for producing a food or beverage product having free divalent cation milk protein and plant protein aggregates
CN109982570A (en) Produce the method with the food or beverage products of free bivalent cation protein aggregation
JP7139312B2 (en) Micronized whey protein and method for producing same
Niakousari et al. Conventional emulsions
Zhang et al. Soy protein particles as stabilizers of heat-stable O/W emulsions with 20% protein content
JP6771335B2 (en) Method for producing soy protein for food composition and method for producing food composition
JPH04227842A (en) Semitransparent thixotropic aqueous gel containing non-granular denatured protein, its manufacture and food and cosmetics containing said gel
CN116369494A (en) A method for preparing plant-based mayonnaise using soybean protein fibril-pectin complex
JP2016002060A (en) Gel nutrition composition
JPH10155433A (en) Composition for food compounded with emulsified gelatinous fats and oils and food compounded with emulsified gelatinous fats and oils
CN106615141A (en) Milk protein-anionic polysaccharide emulsification stabilizer and application thereof
WO2015146151A1 (en) Nutrition composition
CN102291994A (en) Oil-in-water-type emulsion having milk flavor improved by calcium ion
KR20010069608A (en) Water dispersive mastic gum compound and preparation method thereof
CN104323235B (en) Double protein co-emulsion system and its preparation method and application
CN105077381B (en) Method for producing unsaturated fatty acid-containing fat powder

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20190702

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20200424

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20200526

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20200720

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20200915

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20200929

R150 Certificate of patent or registration of utility model

Ref document number: 6771335

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250