JPS5921364A - Preparation of soybean or soybean protein having improved quality - Google Patents

Preparation of soybean or soybean protein having improved quality

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Publication number
JPS5921364A
JPS5921364A JP57132900A JP13290082A JPS5921364A JP S5921364 A JPS5921364 A JP S5921364A JP 57132900 A JP57132900 A JP 57132900A JP 13290082 A JP13290082 A JP 13290082A JP S5921364 A JPS5921364 A JP S5921364A
Authority
JP
Japan
Prior art keywords
soybean
ethanol
alkali
odor
alcohol
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
JP57132900A
Other languages
Japanese (ja)
Other versions
JPS613469B2 (en
Inventor
Shigehide Matsuzaki
成秀 松崎
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP57132900A priority Critical patent/JPS5921364A/en
Publication of JPS5921364A publication Critical patent/JPS5921364A/en
Publication of JPS613469B2 publication Critical patent/JPS613469B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To perpare soybean or soybean protein having improved quality, free from soybean smell and unagreeable odor and taste, by extracting soybean or soybean protein with a liquid obtained by the alkali- and active carbon-treatment of an alcohol-containing solvent used in extraction process. CONSTITUTION:Soybean or soybean protein is extracted with an alcohol-containing solvent to improve the quality of the soybean or the soybean protein. The circulation ethanol containing the components having unagreeable taste and odor is introduced through the line 1 into the thermal reactor 3, and an alkali is introduced through the line 2 into the reactor in the form of an aqueous solution. The amount of the alkali is >=0.1wt% based on ethanol. The mixture of the ethanol and alkali is mixed under heating at 40-82 deg.C to react a part of the ill-odor component with the alkali. After the completion of the reaction, the reaction solution is transferred to the concentrator 4, and distilled under atmospheric or reduced pressure. The concentrated residue is discharged from the outlet 5, and the ethanol vapor is condensed in the condenser 6. The condensed ethanol is passed through the active carbon adsorption column 7 to remove the remaining ill-odor component completely.

Description

【発明の詳細な説明】 本発明は大豆又は脱脂大豆等植物種子の有機溶剤抽出法
による品質改善法に関し、更に詳しくは大豆又は脱脂大
豆に低級アルコール含有有機溶剤を接触せしめ、使用溶
剤を回収精製する、大豆臭及び異臭味のない大豆蛋白製
造法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for improving the quality of plant seeds such as soybeans or defatted soybeans using an organic solvent extraction method. The present invention relates to a method for producing soybean protein that is free from soybean odor and off-flavor taste.

最近、植物蛋白特に大豆蛋白の食品としての重要度が増
すに従い、大豆のアルコール処理が注目され重要視され
てきている。
Recently, as the importance of plant proteins, particularly soybean proteins, as foods has increased, alcohol treatment of soybeans has been attracting attention and importance.

従来より大豆又は脱脂大豆にメタノール、エタノール、
プロパノール等含水低級アルコール或いは上記低級アル
コールを含んだ有機溶剤を接触せしめると大豆特有の臭
い、風味、及び着色物質が抽出除去され、得られる大豆
製品の品質が大巾に改善されることは良く知られている
Conventionally, soybeans or defatted soybeans are mixed with methanol, ethanol,
It is well known that when brought into contact with hydrous lower alcohols such as propanol or organic solvents containing the above lower alcohols, the odor, flavor, and coloring substances peculiar to soybeans are extracted and removed, and the quality of the resulting soybean products is greatly improved. It is being

この方法を工業的に実施する場合には経済上大豆に付着
した溶剤及び使用済みの溶剤から溶剤を蒸留回収し循環
使用することが不可欠であるが、溶剤を長時間循環使用
すると単純な蒸留法では除去できない。しかも大豆特有
の不快臭とは異質の異臭味成分が溶剤中に徐々に蓄積さ
れ、大豆特有の不快臭、風味、色調の点では満足のいく
製品が得られても上記異臭味成分が最終製品に吸着し製
品の食品用途としての商品価値を大いに損ねることにな
る。
If this method is to be carried out industrially, it is economically necessary to distill and recover the solvent from the solvent attached to the soybeans and the used solvent and reuse it, but if the solvent is used repeatedly for a long period of time, it is necessary to use the simple distillation method. It cannot be removed. In addition, off-flavor and taste components that are different from the unpleasant odor peculiar to soybeans gradually accumulate in the solvent, and even if a product that is satisfactory in terms of the unpleasant odor, flavor, and color tone peculiar to soybeans is obtained, the above-mentioned off-odor and taste components are present in the final product. This will greatly reduce the commercial value of the product as a food product.

このような循環溶剤の汚染による品質低下を防止する方
法は種々考えられるが、簡単に有効に防止する満足すべ
き方法は無い。
Various methods can be considered to prevent quality deterioration due to contamination of the circulating solvent, but there is no satisfactory method that simply and effectively prevents it.

この異臭味成分を除去する方法としては製品を水蒸気処
理する方法(特開昭54−101456)があるが、こ
れは製品大豆蛋白の品質及びコスト的に満足すべきもの
でなく、また別方法として循環使用アルコールに加水し
有臭成分の比揮発度を増大させ、蒸留分離する方法が考
えられた(特公昭56−36900)、しかし、この方
法は溶剤中の異臭味成分を除去できる点においては優れ
たものであるが装置が複雑になること、コスト的にも必
ずしも満足すべき方法ではなく、より経済的かつ簡便な
脱臭法が望まれていた。
There is a method of steam-treating the product (Japanese Unexamined Patent Publication No. 54-101456) to remove this off-flavor and taste component, but this method is not satisfactory in terms of the quality and cost of the soybean protein product, and another method is recycling. A method of increasing the specific volatility of odorous components by adding water to the alcohol used and separating them by distillation was considered (Japanese Patent Publication No. 56-36900), but this method is superior in that it can remove off-flavor components from the solvent. However, this method requires a complicated device and is not necessarily satisfactory in terms of cost, and a more economical and simple deodorizing method has been desired.

本発明の目的は循環用アルコール中の微量異臭味成分を
簡便かつ有効に除去し、優れた風味を有する大豆蛋白製
品を製造取得する為の新規な方法を提供することにある
An object of the present invention is to provide a new method for easily and effectively removing trace amounts of off-flavor components from circulating alcohol and for producing and obtaining soybean protein products with excellent flavor.

本発明者は、かかる目的を達成すべく種々研究した結果
、(1)抽出処理したアルコール含有溶剤にアルカリを
アルコールに対して0.1重量%以上添加し加熱処理す
る工程、及び(2)抽出処理したアルコール含有溶剤を
活性炭で吸着処理する工程の両工程を、その順序を問う
ことなく施して得られたアルコール水溶液を用いて大豆
又は大豆蛋白を抽出処理することにより異臭成分を分離
除去できることを発見し本発明を完成するに至った。
As a result of various studies to achieve the above object, the present inventor found that (1) a step of adding 0.1% by weight or more of an alkali to the alcohol to an extraction-treated alcohol-containing solvent and heat-treating the same, and (2) an extraction process. It has been shown that off-flavor components can be separated and removed by extracting soybeans or soybean protein using an aqueous alcohol solution obtained by performing both steps of adsorbing the treated alcohol-containing solvent with activated carbon, regardless of their order. This discovery led to the completion of the present invention.

即ち本発明は抽出処理したアルコール含有溶剤中に蓄積
する異臭味成分なアルカリ処理と活性炭処理を組み合わ
せることにより分離除去することを特徴とする品質の改
善された大豆又は大豆蛋白製品の製造法である。
That is, the present invention is a method for producing soybeans or soybean protein products with improved quality, which is characterized in that off-flavor and taste components that accumulate in an alcohol-containing solvent subjected to extraction treatment are separated and removed by a combination of alkali treatment and activated carbon treatment. .

脱脂大豆なエタノールで処理し大豆蛋白製品を製造する
場合を例として本発明の方法について設明すると、まず
脱脂大豆は40重量%から99重量%の含水エタノール
で抽出処理され、抽出物を含んだエタノールは蒸留等に
より抽出物を除き濃度調整の後循環使用される。また溶
剤を付着した大豆は脱溶剤処理され、回収したエタノー
ルは循環用に供給され、大豆は粉砕され色調および風味
の改善された製品となる。
The method of the present invention will be explained by taking as an example a case where a soybean protein product is produced by treating defatted soybeans with ethanol. First, defatted soybeans are extracted with 40% to 99% by weight ethanol to remove the extracts. Ethanol is used for circulation after removing extracts by distillation etc. and adjusting the concentration. In addition, soybeans contaminated with solvent are treated to remove the solvent, the recovered ethanol is supplied for circulation, and the soybeans are ground into products with improved color and flavor.

上記回収された循環用エタノールは外見上は無色透明で
純粋な含水エタノールと全く変わりがないが大豆臭とは
異なる異臭味成分を含んでおり、この溶剤で大豆を処理
した際、大豆特有の臭と味は改善されるものの溶剤中の
異臭味成分が大豆に吸着され、最終製品にまで残存し品
質的に満足のいく製品は得られない。
The recycled ethanol recovered above looks colorless and transparent and has no difference from pure hydrated ethanol, but it contains an off-flavor component that is different from the soybean odor, and when soybeans are treated with this solvent, the soybean-specific odor Although the taste is improved, the off-flavor components in the solvent are adsorbed by the soybeans and remain in the final product, making it impossible to obtain a product with satisfactory quality.

本発明者は、この異臭について鋭意検討した結果、異臭
は単一成分の臭いではなく、複数の微量成分からなる臭
いであり、さらにはこの臭いは刺激臭と腐敗臭に大きく
分けることができ、前者は主にアルデヒド・エステル類
、後者はアミン系物質であることを発見した。
As a result of intensive studies on this off-odor, the inventor of the present invention discovered that the off-odor is not the odor of a single component, but is an odor composed of multiple trace components, and furthermore, this odor can be broadly divided into irritating odor and putrid odor. It was discovered that the former are mainly aldehydes and esters, and the latter are amine-based substances.

本発明の方法は(1)抽出処理したアルコール含有溶剤
に刺激臭を取り除く為に、アルカリをアルコールに対し
て0.1%以上添加して加熱処理する工程、及び(2)
抽出処理したアルコール含有溶剤に腐敗臭を取り除く為
に活性炭で吸着処理を行なう工程の両工程を、その順序
を問うことなく施してアルコール水溶液中の異臭成分を
完全に取り除くものである。
The method of the present invention includes (1) a step of adding 0.1% or more of alkali to the alcohol and heat-treating the extracted alcohol-containing solvent in order to remove the irritating odor; and (2)
The process of adsorbing the extracted alcohol-containing solvent with activated carbon to remove the putrid odor is performed in any order to completely remove the off-flavor components in the alcohol aqueous solution.

まず、アルカリ処理工程は、水酸化ナトリウム、水酸化
カルシウム、水酸化カリウムなどのアルカリ、またはこ
れらのアルカリ水溶液を用いる。アルカリの添加量は0
.1%以上が好ましい。0.1%未満では風味改善の効
果はあまり認められない。
First, the alkali treatment step uses an alkali such as sodium hydroxide, calcium hydroxide, potassium hydroxide, or an aqueous alkali solution thereof. The amount of alkali added is 0
.. 1% or more is preferable. If the amount is less than 0.1%, the effect of flavor improvement will not be observed much.

アルカリを添加した後、40℃ないし82℃に加熱しつ
つ攪拌し刺激臭成分をアルカリと反応させる。反応溶液
を、好ましくは蒸留してアルカリ及び異臭成分の反応物
な除去する。
After adding the alkali, the mixture is heated to 40° C. to 82° C. and stirred to react the irritating odor components with the alkali. The reaction solution is preferably distilled to remove alkali and off-flavor components.

次の活性炭処理工程で用いる活性炭の使用量は、アルコ
ールに対して5%以上用いるのが好ましく、使用後の活
性炭は通常の再生法で再生し循環使用することが可能で
ある。
The amount of activated carbon used in the next activated carbon treatment step is preferably 5% or more based on the alcohol, and the activated carbon after use can be regenerated by a normal regeneration method and recycled.

装置としては特殊なものは必要としないが、第一図に示
すような装置が好ましい。第一図においてAはアルカリ
処理、Bは活性炭処理である。またこの工程は¥A¥と
¥B¥の順序を入れ替えても同様の効果を示す。
Although no special equipment is required, an equipment as shown in Figure 1 is preferred. In Figure 1, A indicates alkali treatment and B indicates activated carbon treatment. Moreover, this process shows the same effect even if the order of ¥A¥ and ¥B¥ is changed.

第一図中¥1¥は蒸留後のエタノール供給口、¥2¥は
アルカリの供給口、¥3¥は加熱反応機、¥4¥は蒸発
濃縮缶、¥5¥は濃縮残渣排出口、¥6¥はコンデンサ
ー、¥7¥は活性炭吸着塔、¥8¥は精製エタノール排
出口である。
In Figure 1, ¥1 is the ethanol supply port after distillation, ¥2 is the alkali supply port, ¥3 is the heating reactor, ¥4 is the evaporative concentrator, ¥5 is the concentration residue discharge port, 6 yen is a condenser, 7 yen is an activated carbon adsorption tower, and 8 yen is a purified ethanol outlet.

異臭味成分を含んだ循環用エタノールは供給口¥1¥か
ら加熱反応機¥3¥に供給され、アルカリはエタノール
に対し0.1重量%以上になるよう水溶液で供給口¥2
¥より供給される。さらにこの混合液は40℃〜82℃
に加熱攪拌され、異臭成分の一部をアルカリと反応させ
る。
Circulating ethanol containing off-flavor components is supplied from the supply port ¥1 to the heating reactor at ¥3, and the alkali is supplied in an aqueous solution to the ethanol at a concentration of 0.1% by weight or more at the supply port ¥2.
Supplied from ¥. Furthermore, this mixed liquid is 40℃~82℃
The mixture is heated and stirred to cause some of the off-flavor components to react with the alkali.

反応終了後、反応溶液は濃縮缶4に供給され、常圧もし
くは減圧下で蒸留し濃縮残渣は排出口¥5¥より排出さ
れ、エタノール蒸気はコンデンザー¥6¥で凝集せられ
る。
After the reaction is completed, the reaction solution is supplied to the concentrator 4 and distilled under normal pressure or reduced pressure, the concentrated residue is discharged from the outlet, and the ethanol vapor is condensed in the condenser.

次に凝集エタノールを活性炭吸着塔¥7¥に供給し残り
の異臭成分を完全に除去する。循環用エタノールは全量
について精製する必要はなく、要求される製品の品質に
応じてその割合は決められる。
Next, the coagulated ethanol is fed to an activated carbon adsorption tower for 7 yen to completely remove the remaining off-flavor components. It is not necessary to purify the entire amount of ethanol for circulation; the proportion is determined depending on the required quality of the product.

以上脱脂大豆をエタノールで抽出処理する方法について
説明したが、本発明は脱脂大豆のみに限らず大豆及び大
豆を原料として製造される大豆蛋白製品など植物種子の
アルコール抽出処理における品質改善法として適用され
る。尚、アルコールとしてはエタノールが最も好ましい
がその他メタノール、プロパノール、ブタノール等低級
アルコールも利用できる。
Although the method for extracting defatted soybeans with ethanol has been described above, the present invention is applicable not only to defatted soybeans but also as a quality improvement method in the alcohol extraction treatment of plant seeds such as soybeans and soybean protein products manufactured using soybeans as raw materials. Ru. The most preferred alcohol is ethanol, but other lower alcohols such as methanol, propanol, and butanol can also be used.

本発明の方法で処理して得られる大豆又は大豆蛋白製品
は、従来の方法で得られるものがエタノール中の異臭味
成分で汚染され風味が劣り、商品価値が損なわれるのに
対し、品質の低下は全くなく、製品及び循環用エタノー
ルの官能検査でも異臭味は全く検知されず品質の改善さ
れた優れたものである。
The soybeans or soybean protein products obtained by the method of the present invention have a lower quality, whereas those obtained by the conventional method are contaminated with off-flavor components in ethanol and have inferior flavor and loss of commercial value. No off-odor taste was detected in the sensory tests of the product and circulating ethanol, indicating that the quality has been improved.

実施例1 脱脂大豆フレーク(280kg/hr)を79重量%エ
タノール溶剤比2(560kg/hr)で温度50℃に
おいて連続向流抽出した。得られた抽出エタノールミセ
ラは濃縮機で常圧下濃縮され、残渣を72kg/hr、
エタノールを429kg/hr得た。また溶剤を含んだ
大豆フレークは脱溶剤されフレーク218kg/hrと
エタノール123kg/hrを得た。両工程より回収し
たエタノールは混合され 、次の脱臭工程に供給される
が、このアルコールは無色透明ではあるが異臭味成分を
含んでいた。
Example 1 Defatted soybean flakes (280 kg/hr) were subjected to continuous countercurrent extraction with 79 wt% ethanol solvent ratio 2 (560 kg/hr) at a temperature of 50°C. The obtained extracted ethanol miscella was concentrated in a concentrator under normal pressure, and the residue was collected at 72 kg/hr.
429 kg/hr of ethanol was obtained. Further, the soybean flakes containing the solvent were removed to obtain 218 kg/hr of flakes and 123 kg/hr of ethanol. The ethanol recovered from both processes was mixed and supplied to the next deodorizing process, but although this alcohol was clear and colorless, it contained components with off-flavors and tastes.

回収したエタノールはまずエタノール溶液に対し0.5
%の水酸化ナトリウム2.8kg/hrと加熱反応缶3
で混合され、70℃で30分間加熱攪拌した。
The recovered ethanol is first diluted with 0.5% of the ethanol solution.
% of sodium hydroxide 2.8 kg/hr and heating reaction vessel 3
The mixture was heated and stirred at 70° C. for 30 minutes.

反応溶液はついで濃縮缶で常圧下濃縮され、残渣として
7.2kg/hrエタノール蒸気はコンデンサー6で凝
縮され548kg/hrを得た。
The reaction solution was then concentrated in a concentrator under normal pressure, and 7.2 kg/hr of ethanol vapor as a residue was condensed in condenser 6 to obtain 548 kg/hr.

このエタノールは刺激臭は消えているが依然として腐敗
臭に似た臭いを有している。アルカリ処理エタノールは
次に活性炭吸着塔7に供給され異臭味のない精製エタノ
ールを得、79重量%に濃度調整を行った後抽出溶剤と
して循環使用された。
Although the pungent odor of this ethanol has disappeared, it still has an odor similar to putrid odor. The alkali-treated ethanol was then fed to the activated carbon adsorption tower 7 to obtain purified ethanol with no off-flavor or taste, and after adjusting the concentration to 79% by weight, it was recycled as an extraction solvent.

これに対し回収したエタノールを脱臭精製することなく
循環使用し、脱脂大豆を同条件下で処理した。
On the other hand, the recovered ethanol was recycled without being deodorized and purified, and the defatted soybeans were treated under the same conditions.

この両方法で得られた大豆フレークを専門パネラー11
名により5点評価による官能検査を行った。
Expert panel 11 said that soybean flakes obtained by both methods were
A sensory test was conducted using a 5-point evaluation.

結果を表1に示す。The results are shown in Table 1.

第1表 大豆製品の官能検査 (評価基準:0点・・・異臭味を全く感じない5点・・
・異臭味が極めて強い) 第1表が示すようにエタノールの脱臭精製を行っていな
い従来の系で得られた製品では明らかに異臭味の残存が
認められ、本発明の脱臭精製を付加した系では異臭味を
ほとんど感じない程度まで改善された優れたものであっ
た。
Table 1: Sensory test for soybean products (evaluation criteria: 0 points...5 points: no abnormal odor or taste...
・Extremely strong off-odor and taste) As shown in Table 1, products obtained using the conventional system that does not perform ethanol deodorization and purification clearly have residual off-odor and taste. It was an excellent product, with the odor and taste improved to the extent that it was almost unnoticeable.

実施例2 実施例1において脱臭工程の第1工程と第2工程のそれ
ぞれの脱臭効果を調べる目的で次の実験を行った。
Example 2 In Example 1, the following experiment was conducted for the purpose of examining the deodorizing effects of the first and second steps of the deodorizing process.

実験Aでは脱臭精製においてアルカリ処理の第1工程だ
けを採用した 実験Bでは脱臭精製において活性炭処理の第1工程だけ
を採用した 実験Cは実施例1の両工程を採用した場合及び実験Dは
実験Cの両工程の順序を逆にして処理した場合で抽出処
理条件等は実施例1と同様である。
In Experiment A, only the first step of alkaline treatment was used in deodorizing purification. In Experiment B, only the first step of activated carbon treatment was used in deodorizing purification. In Experiment C, both steps of Example 1 were adopted, and in Experiment D. The extraction processing conditions and the like are the same as in Example 1 except that the order of both steps in C is reversed.

結果は第2表に示すようにそれぞれの工程単独では満足
のいく大豆製品は得られず、両工程を組み合わせた系で
は順序を逆にしても異臭味の改善された大豆製品が得ら
れた。
As shown in Table 2, a satisfactory soybean product could not be obtained by using each process alone, but a soybean product with improved off-flavor and taste was obtained by combining both processes even when the order was reversed.

実施例3 アルカリ処理工程において添加する水酸化ナトリウム量
の影響を調べる目的で次の実験を行った。
Example 3 The following experiment was conducted for the purpose of investigating the influence of the amount of sodium hydroxide added in the alkali treatment step.

抽出は実施例1の条件に従って行い、回収したエタノー
ルは水酸化ナトリウム0.02%、0.05%、0.1
%、0.5%、2%の5水準添加し70℃で30分間ア
ルカリ処理を行った。反応液は蒸留精製し次に活性炭処
理を行い循環使用した。
Extraction was performed according to the conditions of Example 1, and the recovered ethanol was extracted with sodium hydroxide at 0.02%, 0.05%, and 0.1%.
%, 0.5%, and 2%, and alkali treatment was performed at 70° C. for 30 minutes. The reaction solution was purified by distillation, then treated with activated carbon, and recycled for use.

この5水準での実験で得られた大豆フレークについて5
点評価による官能検査を行った。
About the soybean flakes obtained in the experiment at these 5 levels
A sensory test was conducted using point evaluation.

結果を第3表に示す。The results are shown in Table 3.

−361− −362− −363− −364−-361- -362- -363- -364-

Claims (1)

【特許請求の範囲】[Claims] 大豆又は大豆蛋白をアルコール含有溶剤で抽出処理して
大豆又は大豆蛋白の品質を改善する方法に於て、(1)
抽出処理したアルコール含有溶剤に、アルカリをアルコ
ールに対して0.1%以上添加して加熱処理する工程及
び(2)抽出処理したアルコール含有溶剤を活性炭で吸
着処理する工程の両工程を、その順序を問うことなく施
して得られたアルコール水溶液を用いて大豆又は大豆蛋
白な抽出処理することを特徴とする品質の改善された大
豆又は大豆蛋白の製造法。
In a method for improving the quality of soybeans or soybean protein by extracting soybeans or soybean protein with an alcohol-containing solvent, (1)
The steps of adding 0.1% or more of alkali to the alcohol to the extracted alcohol-containing solvent and heating it, and (2) adsorbing the extracted alcohol-containing solvent with activated carbon, are carried out in that order. 1. A method for producing soybeans or soybean protein with improved quality, which comprises extracting soybeans or soybean protein using an aqueous alcohol solution obtained by applying any of the following.
JP57132900A 1982-07-29 1982-07-29 Preparation of soybean or soybean protein having improved quality Granted JPS5921364A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57132900A JPS5921364A (en) 1982-07-29 1982-07-29 Preparation of soybean or soybean protein having improved quality

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57132900A JPS5921364A (en) 1982-07-29 1982-07-29 Preparation of soybean or soybean protein having improved quality

Publications (2)

Publication Number Publication Date
JPS5921364A true JPS5921364A (en) 1984-02-03
JPS613469B2 JPS613469B2 (en) 1986-02-01

Family

ID=15092169

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57132900A Granted JPS5921364A (en) 1982-07-29 1982-07-29 Preparation of soybean or soybean protein having improved quality

Country Status (1)

Country Link
JP (1) JPS5921364A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63245648A (en) * 1987-04-01 1988-10-12 Ajinomoto Co Inc Production of soybean food material
EP1506782A1 (en) * 2003-08-11 2005-02-16 I-Hung Chu Vapor fraction from seeds of glycine max (L.) merr. and composition thereof
US7112344B2 (en) 2003-08-11 2006-09-26 I-Hung Chu Vapor fraction from seeds of Glycine max (L.)Merr. and composition thereof
US7282226B2 (en) 2003-08-11 2007-10-16 I-Hung Chu Vapor fraction from seeds of Glycine max (L.) Merr. and composition thereof
KR101284071B1 (en) * 2003-08-11 2013-07-10 추 이-헝 Vapor fraction from seeds of glycine max(l.) merr. and composition thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63245648A (en) * 1987-04-01 1988-10-12 Ajinomoto Co Inc Production of soybean food material
EP1506782A1 (en) * 2003-08-11 2005-02-16 I-Hung Chu Vapor fraction from seeds of glycine max (L.) merr. and composition thereof
US7112344B2 (en) 2003-08-11 2006-09-26 I-Hung Chu Vapor fraction from seeds of Glycine max (L.)Merr. and composition thereof
US7282226B2 (en) 2003-08-11 2007-10-16 I-Hung Chu Vapor fraction from seeds of Glycine max (L.) Merr. and composition thereof
KR101284071B1 (en) * 2003-08-11 2013-07-10 추 이-헝 Vapor fraction from seeds of glycine max(l.) merr. and composition thereof

Also Published As

Publication number Publication date
JPS613469B2 (en) 1986-02-01

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