JP2001017119A - Production of mayonnaise-like food - Google Patents

Production of mayonnaise-like food

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Publication number
JP2001017119A
JP2001017119A JP11195898A JP19589899A JP2001017119A JP 2001017119 A JP2001017119 A JP 2001017119A JP 11195898 A JP11195898 A JP 11195898A JP 19589899 A JP19589899 A JP 19589899A JP 2001017119 A JP2001017119 A JP 2001017119A
Authority
JP
Japan
Prior art keywords
mayonnaise
protein
food
production
soybean protein
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.)
Granted
Application number
JP11195898A
Other languages
Japanese (ja)
Other versions
JP3597083B2 (en
Inventor
Yasunori Sato
康則 佐藤
Yasunobu Saito
康信 齋藤
Kazuko Watanabe
和子 渡辺
Kaori Muroga
香織 室賀
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.)
Nisshin Oil Mills Ltd
Original Assignee
Nisshin Oil Mills 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 Nisshin Oil Mills Ltd filed Critical Nisshin Oil Mills Ltd
Priority to JP19589899A priority Critical patent/JP3597083B2/en
Publication of JP2001017119A publication Critical patent/JP2001017119A/en
Application granted granted Critical
Publication of JP3597083B2 publication Critical patent/JP3597083B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a method for producing mayonnaise-like food with a little decreasing rate in viscosity when compared the one several months after production with the other just after the production, having shape-retaining properties when squeezed out of a mayonnaise vessel. SOLUTION: This production of mayonnaise-like food is to disperse condensed soybean protein obtained by washing de-fatted soybeans with water-containing alcohol in a weak alkaline aqueous solution, apply a protein hydrolase to the solution, treat it to homogenize by maintaining a heating condition after the reaction and obtain refined soybean protein, mix oil and fat, vinegar, a seasoning, etc. with the refined protein and emulsify the mixture.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は特定の方法で得られた大
豆蛋白を卵の代りに乳化剤として用いる粘度安定性のす
ぐれたマヨネーズ様食品の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a mayonnaise-like food having excellent viscosity stability, using soybean protein obtained by a specific method as an emulsifier instead of an egg.

【0002】[0002]

【従来の技術】近年健康のためコレステロールを含まな
い食品に対するニーズが高まってきており、マヨネーズ
についても乳化剤として卵を用いない大豆蛋白を用いた
マヨネーズ様食品の開発がこれまでにも試みられてき
た。すなわちアルコール変性された大豆蛋白質をプロテ
アーゼで三塩化酢酸可溶化率15〜35%になるまで分
解して可溶化し、不溶物を分離して精製大豆蛋白質を得
た後、この精製大豆蛋白質に油脂、食酢、調味料等を混
合乳化することからなるマヨネーズ様食品の製造法(特
開昭56−26171)や、アルコール変性された大豆
蛋白質の水分散液に中性又はアルカリ性プロテアーゼを
作用させ三塩化酢酸可溶化率約8〜15%になるまで部
分加水分解を行わせ、酵素の失活後不溶物を除去して精
製大豆蛋白質を得た後、この精製大豆蛋白質に該大豆蛋
白の含有量が組成物の全重量に対して乾物として約0.
5%をこえ且つ2.5重量%未満となる様に油脂、食
酢、調味料等を混合し乳化することからなる、スクイズ
性のすぐれたマヨネーズ様食品の製造法(特開昭56−
158073)が提案されている。
2. Description of the Related Art In recent years, there has been an increasing demand for cholesterol-free foods for health reasons. For mayonnaise, development of mayonnaise-like foods using soy protein without using eggs as an emulsifier has been attempted. . That is, alcohol-denatured soybean protein is decomposed with a protease until the solubilization rate of acetic acid trichloride becomes 15 to 35%, solubilized, and insolubles are separated to obtain a purified soybean protein. For producing mayonnaise-like foods by mixing and emulsifying vinegar, seasonings, etc. (JP-A-56-26171), or by allowing a neutral or alkaline protease to act on an aqueous dispersion of alcohol-denatured soybean protein. After partial hydrolysis is carried out until the acetic acid solubilization ratio becomes about 8 to 15%, and after inactivation of the enzyme, insoluble matter is removed to obtain a purified soybean protein, the content of the soybean protein in the purified soybean protein is reduced. Approximately 0.2% as dry matter based on the total weight of the composition.
A method for producing a mayonnaise-like food having excellent squeezing properties, comprising mixing and emulsifying fats and oils, vinegar, seasonings and the like so as to exceed 5% and less than 2.5% by weight (Japanese Patent Laid-Open No. Sho 56-56
158073).

【0003】しかしながら、これらの提案の方法で製造
されたマヨネーズ様食品では、製造直後および製造後時
間経過が少ない時点では粘度が高く、プラスチック容器
などのチューブから押出した時に保型性を有している
が、製造後数ヵ月経過した後では製造直後と比較した粘
度減少率が大きいために粘度が低くなり、チューブから
押出した時に保型性を有しておらず、商品としての価値
が低下する。製造後数ヵ月経過した後の粘度を高く維持
するためには、製造直後の粘度をより高くする必要があ
るが、その場合は粘度が高すぎるために製造時に容器へ
の充填不良が発生するなど、製造に支障をきたすことに
なる。
However, the mayonnaise-like foods produced by these proposed methods have a high viscosity immediately after production and at a point in time after the production is short, and have a shape-retaining property when extruded from a tube such as a plastic container. However, several months after production, the viscosity decreases compared to immediately after production, so the viscosity is low, and when extruded from a tube, it does not have shape retention, reducing its value as a product . In order to maintain a high viscosity several months after production, it is necessary to increase the viscosity immediately after production, but in such a case, the viscosity is too high and filling of the container at the time of production will be defective. , Which would hinder manufacturing.

【0004】[0004]

【発明が解決しようとする課題】本発明は、製造後数ヵ
月経過した後でも製造直後と比較して粘度減少率が小さ
く、チューブから押出した時に保型性を有するマヨネー
ズ様食品の製造方法を提供することを目的としてなされ
たものである。
SUMMARY OF THE INVENTION The present invention relates to a method for producing a mayonnaise-like food which has a small viscosity reduction rate even after several months from the production and has a shape-retaining property when extruded from a tube. It was made for the purpose of providing.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記課題
を解決するため鋭意研究した結果、脱脂大豆を含水アル
コールで洗浄することによって得られる溶剤変性した濃
縮大豆蛋白を弱アルカリ性水溶液に分散させ、蛋白質加
水分解酵素を作用させたのち、加熱して酵素分解反応を
停止し、該加熱状態を維持したまま均質化処理を行って
得られる精製大豆蛋白を使用することによって前記目的
を達成できることを見い出し、本発明を完成するに至っ
たのである。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, dispersed concentrated soybean protein obtained by washing defatted soybeans with aqueous alcohol in a weakly alkaline aqueous solution. The above-mentioned object can be achieved by using purified soybean protein obtained by heating and stopping the enzymatic decomposition reaction after heating the protein hydrolase, and performing homogenization treatment while maintaining the heated state. Thus, the present invention was completed.

【0006】すなわち本発明は、脱脂大豆を含水アルコ
ールで洗浄することによって得られる溶剤変性した濃縮
大豆蛋白を弱アルカリ性水溶液に分散させ、蛋白質加水
分解酵素を作用させたのち、加熱して酵素分解反応を停
止し、該加熱状態を維持したまま均質化処理を行って精
製大豆蛋白を得る第一工程と、この精製大豆蛋白に油
脂、食酢、調味料等を混合し乳化する第二工程よりな
る、製造後数ヵ月経過した後でも製造直後と比較した粘
度減少率が小さいためにチューブから押出した時の保型
性を有するマヨネーズ様食品の製造方法である。
[0006] That is, the present invention is to disperse a solvent-denatured concentrated soybean protein obtained by washing defatted soybeans with hydrous alcohol in a weakly alkaline aqueous solution, act on a protein hydrolase, and then heat to carry out the enzymatic degradation reaction. Stop, the first step of obtaining a purified soy protein by performing homogenization while maintaining the heating state, and a second step of mixing and emulsifying fats and oils, vinegar, seasonings and the like to the purified soy protein, This is a method for producing a mayonnaise-like food having a shape-retaining property when extruded from a tube because the viscosity reduction rate is small compared to immediately after production even after several months after production.

【0007】[0007]

【発明の実施の形態】本発明の方法を詳述すれば次の通
りである。まず、脱脂大豆は原料丸大豆を脱皮してまた
はそのまま圧扁し、溶剤により油を抽出した残渣として
得ることができるが、該方法に限定されるものではな
い。この脱脂大豆は、50〜80W/W%(重量/重量
%を示す。以下同じ)の含水アルコール(アルコールと
しては一般にメタノール、エタノール、イソプロパノー
ルが用いられる。食品製造および取扱い的見地からはエ
タノールが最も好ましい)で公知の方法(浸漬、フラッ
シング等)により前記不純物を洗浄し乾燥する。得られ
る濃縮大豆蛋白は通常65〜75W/W%の蛋白質を含
み、このうち水溶性蛋白質はNSIとして5〜10であ
るから、ネイティブな蛋白質に比べて強度にアルコール
変性を受けている。また脱脂大豆中の有臭成分や色素成
分はほぼ完全に除かれている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The method of the present invention will be described below in detail. First, defatted soybeans can be obtained as a residue obtained by dehulling raw soybeans or pressing them as they are and extracting oil with a solvent, but is not limited to this method. This defatted soybean contains 50 to 80 W / W% (weight / weight%; the same applies hereinafter) of a hydrous alcohol (although methanol, ethanol and isopropanol are generally used as alcohols. From the viewpoint of food production and handling, ethanol is the most common). The impurities are washed and dried by a known method (immersion, flushing, etc.). The obtained concentrated soybean protein usually contains 65 to 75 W / W% protein. Among them, the water-soluble protein has an NSI of 5 to 10 and is more strongly denatured with alcohol than the native protein. Odorous components and pigment components in defatted soybeans are almost completely removed.

【0008】本発明では、この原料(前記溶剤変性した
濃縮大豆蛋白)を5〜20倍重量の水に分散させたの
ち、アンモニア、カセイソーダ、炭酸ナトリウム、好ま
しくはアンモニアでpH7.5〜9.0好ましくはpH
7.5〜8.5に調整する。該溶液を攪拌しながら蛋白
質加水分解酵素例えばニュートラーゼ(ノボノルディス
クバイオインダストリー(株)製、商品名)、アルカラ
ーゼ(同、商品名)などを加えて酵素分解をする。pH
が7.5〜9.0の範囲をはずれると、酵素の加水分解
効率が低下する。酵素分解の温度および時間は任意に選
べるが、長時間の酵素分解による苦味の発生を抑制し、
分解時間をできるだけ短縮するためにその酵素の至適温
度が好ましい。
In the present invention, this raw material (the solvent-denatured concentrated soybean protein) is dispersed in 5 to 20 times the weight of water, and then is adjusted to pH 7.5 to 9.0 with ammonia, caustic soda, sodium carbonate, preferably ammonia. Preferably pH
Adjust to 7.5-8.5. While stirring the solution, a protein hydrolyzing enzyme such as Neutrase (trade name, manufactured by Novo Nordisk Bioindustry Co., Ltd.), Alcalase (trade name, etc.) is added to perform enzymatic degradation. pH
Is out of the range of 7.5 to 9.0, the hydrolysis efficiency of the enzyme decreases. The temperature and time of the enzyme decomposition can be selected arbitrarily, but the generation of bitterness due to long-time enzyme decomposition is suppressed,
The optimal temperature of the enzyme is preferred in order to minimize the decomposition time.

【0009】実際の酵素分解工程の条件は、分解前の蛋
白分散液の濃度、pH、酵素の種類、力価、原料蛋白に
対する添加量、分解時間および温度などのいずれの条件
によっても酵素分解の速さが影響されるため、反応物を
経時的にサンプリングし、その5%三塩化酢酸水溶液に
よる蛋白質の可溶率(TCA可溶率)が8〜35%、好
ましくは15〜25%になるように反応時間を設定す
る。TCA可溶率は8%以下では、溶解性が低くなる。
また、35%を超えると苦味の発生を伴うことがあり、
好ましくない。本発明における酵素分解反応の概略的な
温度および時間は、ニュートラーゼの場合には50±2
℃で約1時間、またアルカラーゼの場合には50±2℃
で約1時間である。
[0009] The actual conditions of the enzymatic digestion step are determined by any conditions such as the concentration of the protein dispersion before degradation, pH, type of enzyme, titer, amount added to the starting protein, degradation time and temperature. Since the speed is affected, the reaction product is sampled with time, and the solubility of the protein (TCA solubility) with a 5% aqueous solution of trichloroacetic acid becomes 8 to 35%, preferably 15 to 25%. The reaction time as follows. If the TCA solubility is 8% or less, the solubility is low.
If it exceeds 35%, bitterness may occur,
Not preferred. The approximate temperature and time of the enzymatic degradation reaction in the present invention is 50 ± 2 for Neutrase.
About 1 hour at 50 ° C or 50 ± 2 ° C for Alcalase
About 1 hour.

【0010】この酵素分解反応は、酵素の失活温度以上
(通常90℃以上)に加熱して停止し、次いで不溶物を
除去することなく、その温度を維持した状態でホモジナ
イザーを用い100kg/cm2以上、好ましくは1000
〜2000kg/cm2の圧力下で均質化および微粒子化処
理する。100kg/cm2未満では均質化処理が不十分で
ある。酵素の失活操作とそれに続く均質化処理は、UH
T(高温瞬間殺菌機)としてAUHT(岩井機械(株)
製、商品名)による高温短時間処理と高圧ホモジナイザ
ーとしてナノマイザーシステム((株)ナノマイザー
製、商品名)を組み合わせることが有利である。
The enzymatic decomposition reaction is stopped by heating to a temperature higher than the inactivation temperature of the enzyme (usually 90 ° C. or higher). Then, the temperature is maintained at 100 kg / cm 2 while maintaining the temperature without removing insolubles. Above, preferably 1000
It is homogenized and atomized under a pressure of 20002000 kg / cm 2. If it is less than 100 kg / cm2, the homogenization treatment is insufficient. Enzyme deactivation and subsequent homogenization were performed using UH
AUHT (Iwai Machinery Co., Ltd.)
It is advantageous to combine a high-temperature and short-time treatment with a Nanomizer system (trade name, manufactured by Nanomizer Co., Ltd.) as a high-pressure homogenizer.

【0011】濃縮大豆蛋白の水分散液の蛋白質加水分解
酵素の反応を停止したのち、均質化処理を行わない場
合、含んでいる水不溶性多糖類(俗称オカラ)が食品中
でザラツキの原因となるため、食品原料として供するに
は支障をきたす場合がある。
When the reaction of the protein hydrolase in the aqueous dispersion of the concentrated soybean protein is stopped and then the homogenization treatment is not performed, the water-insoluble polysaccharide (commonly called okara) contained therein causes graininess in the food. For this reason, there is a case where there is a problem in serving as a food material.

【0012】均質化処理後に得られた精製大豆蛋白溶液
またはこれを噴霧乾燥した精製大豆蛋白粉末からマヨネ
ーズ様食品は次の様にして製造される。精製大豆蛋白溶
液またはこれを噴霧乾燥した精製大豆蛋白粉末を水に還
元したものに食塩、グルタミン酸ナトリウム、核酸系調
味料、砂糖、天然エキス等の調味料、香辛料を加え、さ
らに必要に応じて増粘安定剤を分散溶解させる。食用油
中にはあらかじめ天然色素、香料等を溶解させておくこ
とができる。こうして得られた大豆蛋白溶液と食用油と
をパドルミキサー、ホモミキサー、コロイドミル等の乳
化機を用いて乳化する。次に食酢を加え、さらに乳化機
を用いて乳化する。
From the purified soybean protein solution obtained after the homogenization treatment or the purified soybean protein powder obtained by spray-drying the same, a mayonnaise-like food is produced as follows. To a purified soybean protein solution or a purified soybean protein powder obtained by spray-drying it and reducing it to water, add seasonings and spices such as salt, sodium glutamate, nucleic acid seasonings, sugar and natural extracts, and further increase as necessary. Disperse and dissolve the viscosity stabilizer. In the edible oil, natural pigments, flavors and the like can be dissolved in advance. The soybean protein solution thus obtained and the edible oil are emulsified using an emulsifier such as a paddle mixer, a homomixer, and a colloid mill. Next, vinegar is added and further emulsified using an emulsifier.

【0013】このようにして得られたマヨネーズ様食品
は、粘度安定性がすぐれており、製造後数ヵ月経過した
後でも製造直後と比較した粘度減少率が小さいためにチ
ューブから押出した時の保型性を有する。
The mayonnaise-like food thus obtained has excellent viscosity stability, and even after several months from the production, the viscosity reduction rate is smaller than that immediately after the production, so that the food is preserved when extruded from a tube. It has a mold.

【0014】[0014]

【実施例】以下の実施例および比較例において、%の単
位は特にことわらないかぎり重量基準である。 実施例1 低変性脱脂大豆5kgを60W/W%の含水エタノール3
5kgに浸漬し、50℃で60分間洗浄を行った。これを
濾別し、減圧乾燥機にて70℃で乾燥したのち粉砕して
濃縮大豆蛋白3.4kgを得た。このものの分析値は水
分:7.0%、粗蛋白質:65.8%、NSI:8であ
った。次にこの全量をジャケット付きタンクに移し、3
4リットルの温水を加え攪拌、分散し、アンモニア液で
pH8.0に調整し、液温を50℃とした。アルカラー
ゼ(0.6L)10.2gを加えて50℃で60分間作
用させ、その後AUHTで125℃にて5秒間加熱処理
して反応停止した。この時、TCA可溶率は18%であ
った。それに続いてナノマイザーシステムで1000kg
/cm2にて均質化処理を行い、次に噴霧乾燥して3.2
kgの精製大豆蛋白Aを得た。これは、大豆臭もなく、色
調も明るい白色で水に対する分散性および溶解性の高い
ものであった。分析値は、水分:6.0%、粗蛋白質:
65.3%、NSI:72であった。この精製大豆蛋白
Aを用いて、次の配合に従ってマヨネーズ様食品Aを製
造した。 綿実サラダ油 550g 食酢 70g 調味料 50g 香辛料 5g 精製大豆蛋白A 20g 増粘安定剤 5g 天然色素 2g 水 298g 調味料、香辛料、精製大豆蛋白A、増粘安定剤はあらか
じめ水に分散溶解し、これにあらかじめ天然色素を溶解
させておいた綿実サラダ油を滴加してホモミキサーで乳
化させ、次いで食酢を添加してさらに乳化を続けマヨネ
ーズ様食品Aを1kg得た。
EXAMPLES In the following Examples and Comparative Examples, the unit of% is based on weight unless otherwise specified. Example 1 Low-denatured defatted soybeans (5 kg) were added to 60 W / W% aqueous ethanol 3
It was immersed in 5 kg and washed at 50 ° C. for 60 minutes. This was separated by filtration, dried at 70 ° C. in a vacuum dryer, and then crushed to obtain 3.4 kg of concentrated soybean protein. The analysis value of this product was: water: 7.0%, crude protein: 65.8%, NSI: 8. Next, transfer the whole amount to the jacketed tank,
4 liters of warm water was added, stirred and dispersed, adjusted to pH 8.0 with an ammonia solution, and the solution temperature was adjusted to 50 ° C. 10.2 g of Alcalase (0.6 L) was added and the mixture was allowed to act at 50 ° C. for 60 minutes, and then heat-treated at AUHT at 125 ° C. for 5 seconds to terminate the reaction. At this time, the TCA solubility was 18%. Followed by 1000kg with Nanomizer system
/ Cm 2 and then spray dried to 3.2
kg of purified soy protein A was obtained. It had no soybean odor, bright white color, and high dispersibility and solubility in water. The analysis values were as follows: water: 6.0%, crude protein:
65.3%, NSI: 72. Using this purified soybean protein A, mayonnaise-like food A was produced according to the following formulation. Cottonseed salad oil 550g Vinegar 70g Seasoning 50g Spice 5g Refined soy protein A 20g Thickening stabilizer 5g Natural pigment 2g Water 298g Seasoning, spice, purified soy protein A and thickening stabilizer are dispersed and dissolved in water in advance, and Cottonseed salad oil in which a natural pigment was previously dissolved was added dropwise and emulsified with a homomixer. Then, vinegar was added and emulsification was further continued to obtain 1 kg of mayonnaise-like food A.

【0015】比較例1 実施例1と同様の方法により濃縮大豆蛋白を得、酵素分
解反応を行い、加熱処理にて酵素反応を停止した。次に
遠心分離によって不溶物を除去し、噴霧乾燥して2.1
kgの精製大豆蛋白Bを得た。分析値は、水分:6.0
%、粗蛋白質:73.3%、NSI:86であった。こ
の精製大豆蛋白Bを用いて実施例1と同様の方法で、次
の配合に従ってマヨネーズ様食品Bを1kg得た。ここ
で、精製大豆蛋白Bの配合量は、実施例1における精製
大豆蛋白Aの配合量と、粗蛋白質含有量が等しくなるよ
うに調整した。 綿実サラダ油 550g 食酢 70g 調味料 50g 香辛料 5g 精製大豆蛋白B 17.8g 増粘安定剤 5g 天然色素 2g 水 300.2g
Comparative Example 1 A concentrated soybean protein was obtained in the same manner as in Example 1, an enzymatic decomposition reaction was carried out, and the enzymatic reaction was stopped by heat treatment. Next, insoluble materials were removed by centrifugation, and spray-dried to 2.1.
kg of purified soy protein B was obtained. The analysis value was as follows: water: 6.0
%, Crude protein: 73.3%, NSI: 86. Using this purified soybean protein B, 1 kg of mayonnaise-like food B was obtained in the same manner as in Example 1 according to the following formulation. Here, the blending amount of the purified soybean protein B was adjusted so that the blending amount of the purified soybean protein A in Example 1 was equal to the crude protein content. Cottonseed salad oil 550 g Vinegar 70 g Seasoning 50 g Spice 5 g Purified soy protein B 17.8 g Thickening stabilizer 5 g Natural pigment 2 g Water 300.2 g

【0016】(評価)マヨネーズ様食品Aおよびマヨネ
ーズ様食品Bを250gづつプラスチック容器に充填
し、製造直後および20℃3ヵ月保存後の粘度測定とチ
ューブから押出した時の保型性評価を行った。その結果
を第1表に示す。
(Evaluation) Each of 250 g of mayonnaise-like food A and mayonnaise-like food B was filled in a plastic container, and the viscosity was measured immediately after production and after storage at 20 ° C. for 3 months, and the shape retention when extruded from a tube was evaluated. . Table 1 shows the results.

【0017】[0017]

【表1】 [Table 1]

【0018】即ちマヨネーズ様食品Bのように均質化処
理を行わず遠心分離によって不溶物を除去した精製大豆
蛋白を用いて製造したものは、製造後数ヵ月経過した後
では製造直後と比較した粘度減少率が大きいためにチュ
ーブから押出した時の保型性を有せず、逆にマヨネーズ
様食品Aのように均質化処理を行った精製大豆蛋白を用
いて製造したものは、製造後数ヵ月経過した後でも製造
直後と比較した粘度減少率が小さいためにチューブから
押出した時の保型性を有する。
That is, as in the case of mayonnaise-like food B, the one produced using purified soybean protein from which insoluble matter has been removed by centrifugation without performing homogenization treatment has a viscosity that is several months after the production compared to that immediately after the production. Due to the large reduction rate, it did not have a shape retention property when extruded from a tube. Conversely, those produced using purified soybean protein that had been subjected to homogenization treatment, such as mayonnaise-like food A, were several months after production. Even after the lapse of time, it has a shape retention property when extruded from a tube because the viscosity reduction rate is smaller than that immediately after production.

【0019】[0019]

【発明の効果】本発明によるマヨネーズ様食品は、製造
後数ヵ月経過した後でも製造直後と比較して粘度減少率
が小さく、チューブから押出した時に保型性を有してい
る。
The mayonnaise-like food according to the present invention has a small viscosity reduction rate even after several months from the production, even after several months from the production, and has a shape retaining property when extruded from a tube.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4B047 LB09 LE03 LG07 LG10 LG40 LG57 LG62 LG64 LP03 LP05 LP18  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4B047 LB09 LE03 LG07 LG10 LG40 LG57 LG62 LG64 LP03 LP05 LP18

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 脱脂大豆を含水アルコールで洗浄した濃
縮大豆蛋白を弱アルカリ性水溶液に分散させ、蛋白質加
水分解酵素を作用させたのち、加熱して酵素分解反応を
停止し、不溶物を除去することなく、均質化処理を行っ
て精製大豆蛋白を得る第一工程と、この精製大豆蛋白に
油脂、食酢、調味料を混合し乳化する第二工程よりな
る、粘度安定性のすぐれたマヨネーズ様食品の製造方
法。
1. A method in which concentrated soybean protein obtained by washing defatted soybeans with hydrous alcohol is dispersed in a weakly alkaline aqueous solution, and a protease is allowed to act thereon, followed by heating to stop the enzymatic decomposition reaction and remove insolubles. Without, the first step of obtaining a purified soy protein by performing homogenization treatment, and a second step of mixing and emulsifying fats and oils, vinegar, and seasonings with this purified soy protein, a mayonnaise-like food with excellent viscosity stability Production method.
【請求項2】 濃縮大豆蛋白を弱アルカリ性水溶液に分
散させたときのpHが7.5から9.0である請求項1
記載のマヨネーズ様食品の製造法。
2. The pH of the concentrated soybean protein when dispersed in a weakly alkaline aqueous solution is 7.5 to 9.0.
A method for producing the mayonnaise-like food according to the above.
【請求項3】 濃縮大豆蛋白を弱アルカリ性水溶液に分
散させ、蛋白質加水分解酵素を作用させたのち、加熱し
て酵素分解反応を停止する時期が、5%三塩化酢酸水溶
液による蛋白質の溶解率(TCA可溶率)が8〜35%
である請求項1記載のマヨネーズ様食品の製造法。
3. A method in which concentrated soybean protein is dispersed in a weakly alkaline aqueous solution, a protease is allowed to act on the dispersion, and then the enzymatic degradation reaction is stopped by heating. TCA solubility) 8-35%
The method for producing a mayonnaise-like food according to claim 1, wherein
JP19589899A 1999-07-09 1999-07-09 Production method of mayonnaise-like food Expired - Lifetime JP3597083B2 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002003814A1 (en) * 2000-07-10 2002-01-17 Tajimaya Foods Co., Ltd. Mayonnaise-like foods and process for producing the same
WO2003101220A1 (en) * 2002-05-31 2003-12-11 Isyokudougensya Co.,Ltd Pulse paste, process for producing the same and processed food from the pulse paste
WO2004047549A1 (en) * 2002-11-22 2004-06-10 Cerestar Holding B.V. Process for preparing microbial stable protein suspensions
WO2005051099A1 (en) * 2003-11-28 2005-06-09 Ishokudougensha., Inc Food material made from beans, method of producing the same and processed food with the use of the food material made from beans
JP2015073476A (en) * 2013-10-09 2015-04-20 キユーピー株式会社 Mayonnaise-like seasoning

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002003814A1 (en) * 2000-07-10 2002-01-17 Tajimaya Foods Co., Ltd. Mayonnaise-like foods and process for producing the same
US7029719B1 (en) 2000-07-10 2006-04-18 Tajimaya Foods Co., Ltd. Mayonnaise-like food and method of manufacturing the same
WO2003101220A1 (en) * 2002-05-31 2003-12-11 Isyokudougensya Co.,Ltd Pulse paste, process for producing the same and processed food from the pulse paste
WO2004047549A1 (en) * 2002-11-22 2004-06-10 Cerestar Holding B.V. Process for preparing microbial stable protein suspensions
WO2005051099A1 (en) * 2003-11-28 2005-06-09 Ishokudougensha., Inc Food material made from beans, method of producing the same and processed food with the use of the food material made from beans
JP2015073476A (en) * 2013-10-09 2015-04-20 キユーピー株式会社 Mayonnaise-like seasoning

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