JPS6057822B2 - Method for producing soybean flour from which odor components have been removed - Google Patents
Method for producing soybean flour from which odor components have been removedInfo
- Publication number
- JPS6057822B2 JPS6057822B2 JP53040912A JP4091278A JPS6057822B2 JP S6057822 B2 JPS6057822 B2 JP S6057822B2 JP 53040912 A JP53040912 A JP 53040912A JP 4091278 A JP4091278 A JP 4091278A JP S6057822 B2 JPS6057822 B2 JP S6057822B2
- Authority
- JP
- Japan
- Prior art keywords
- alcohol
- soybean flour
- odor components
- condensate
- water
- 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.)
- Expired
Links
Landscapes
- Beans For Foods Or Fodder (AREA)
Description
【発明の詳細な説明】
本発明は、不快な臭いや苦味を除去した大豆粉の製造方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing soybean flour from which unpleasant odor and bitter taste are removed.
大豆蛋白を食品として利用する場合に、特有の不快な臭
いや苦味がそ利用を制約している。When soybean protein is used as food, its unique unpleasant odor and bitterness limit its use.
この不快な臭い並びに苦味成分(以下臭気成分という。
)を除去する方法は、従来種々の方法が提案されている
が、大豆蛋白質の変性の程度を表示する一つの方法とし
て、水溶性蛋白の含有率の指標であるところのNSI(
NitrogenSolubilityIndex−全
窒素に対する可溶性窒素の百分率)値を低下させること
なく、また脂肪、蛋白等の大豆含有成分を用途に適合し
た品質に維持するとともに、臭気成分を除去した大豆を
蛋白商品として産業上利警、−−リI 1畔、1目4岬
4゛−i”一であつた。従来、臭気成分を除去する方法
としては、生大豆または粉末とした大豆粉を、乾熱で加
熱処理する方法、蒸熱処理する方法またアルコール等親
水性溶剤或いはベンジン等非親水性溶剤を用いて、臭気
成分を抽出除去する方法等が知られている。This unpleasant odor and bitter components (hereinafter referred to as odor components).
) has been proposed in the past, but one way to indicate the degree of denaturation of soybean protein is to use NSI (
While maintaining the quality of soybean-containing components such as fat and protein to meet the intended use without reducing the NitrogenSolubilityIndex (percentage of soluble nitrogen to total nitrogen), soybeans from which odor components have been removed can be used for industrial purposes as protein products. The conventional method for removing odor components is to heat-treat raw soybeans or powdered soybean flour with dry heat. Methods such as steam treatment and methods of extracting and removing odor components using hydrophilic solvents such as alcohol or non-hydrophilic solvents such as benzene are known.
しかし、乾熱あるいは蒸熱処理によつて臭気成分を除去
する場合は、蛋白質が過度の処理を受けて変性し、NS
I値が低下することから避けられず、また前記溶剤を使
用する方法法においても、処理温度、゛時間ならびに大
豆に付着した溶剤を最終的に蒸発除去するときの温度、
時間に対応してNSI値が低下するなどの欠点があつた
。本発明は、これらの欠点を改良したものであつて、生
大豆を脱皮、粉砕して得た大豆粉を原料として、これに
アルコール又はアルコール水溶液を加えて、攪拌混合し
、スラリー状態とした後、減圧、加温し、低沸成分を蒸
発除去して臭気成分をアルコール及び水とともに蒸発除
去し、実質的に臭気成分が除去された大豆粉を得る一方
、蒸発凝縮液に含有する水分及び臭気成分を除去し、ア
ルコールの純度を高めて再使用することを特徴とするも
のである。However, when odor components are removed by dry heat or steam treatment, proteins are denatured due to excessive treatment and NS
This is unavoidable since the I value decreases, and even in the method using the above-mentioned solvent, the treatment temperature, the time, and the temperature at which the solvent attached to the soybeans is finally evaporated and removed,
There were drawbacks such as the NSI value decreasing with time. The present invention has improved these drawbacks, and uses soybean flour obtained by dehulling and pulverizing raw soybeans as a raw material, adding alcohol or an alcohol aqueous solution to this, stirring and mixing it to form a slurry. , reduce pressure and heat to evaporate and remove low-boiling components and evaporate odor components together with alcohol and water to obtain soybean flour from which odor components have been substantially removed, while removing moisture and odor contained in the evaporation condensate. It is characterized by removing components, increasing the purity of alcohol, and reusing it.
また上記の処理によれば、臭気成分を除去された大豆粉
のNSI値を実質的に低下せしめない。Further, according to the above treatment, the NSI value of the soybean flour from which odor components have been removed is not substantially lowered.
この蒸発工程においては蛋白質の変性を避けるため、で
きる限り低温度、短時間で処理を完了することが望まし
い。本発明では、100℃以下において蒸発を促進させ
るため、減圧し、蒸発した蒸気を間接冷却型交換器(以
下凝縮器という。In this evaporation step, in order to avoid protein denaturation, it is desirable to complete the process at as low a temperature as possible and in a short time. In the present invention, in order to promote evaporation at temperatures below 100°C, the pressure is reduced and the evaporated vapor is transferred to an indirect cooling type exchanger (hereinafter referred to as a condenser).
)に導いて、冷却凝縮せしめ凝縮液として回収する。こ
の凝縮液にはアルコールを主成分とし、水及び臭気成分
が含まれる。通常、原料大豆粉には、原料生大豆中の含
有水分に基因する水分並びに粉末化工程中に吸湿した水
分を含有し、その量は5〜8重量%程度である。アルコ
ールを用いて上記の処理を行つた場合、この水分の一部
はアルコールと共沸して凝縮液中に移行する。), cooled and condensed, and recovered as a condensate. This condensate has alcohol as its main component, and also contains water and odor components. Normally, the raw soybean flour contains moisture derived from the moisture content in the raw soybean and moisture absorbed during the powdering process, and the amount thereof is about 5 to 8% by weight. When the above treatment is performed using alcohol, a portion of this water is azeotroped with the alcohol and transferred to the condensate.
また臭気成分も、アルコールあるいは水とともに蒸発し
一部は凝縮液中に移行し、残部は凝縮器において凝縮せ
ず不凝縮性ガスとともに真空ポンプの如き真空発生装置
より排出される。従つて凝縮液として回収したアルコー
ルを、そのま)原料アルコールとして繰返し使用した場
合は、漸次アルコールの純分が低下し、かつ水分及び臭
気成分が増加するので、臭気成分の除去効果が低下する
。またアルコールの価格は、大豆粉の価格に比し高価で
あるため、アルコールを高収率にて回収し、これを再使
用することが産業上利用できる要件となる。第1図は本
発明の工程図を示す。The odor components also evaporate together with the alcohol or water, and a portion of the odor components migrates into the condensate, while the remainder does not condense in the condenser and is discharged from a vacuum generating device such as a vacuum pump together with non-condensable gases. Therefore, if the alcohol recovered as a condensate is repeatedly used as raw alcohol, the purity of the alcohol will gradually decrease and the moisture and odor components will increase, resulting in a decrease in the odor component removal effect. Furthermore, since the price of alcohol is higher than that of soybean flour, it is necessary to recover alcohol at a high yield and reuse it for industrial use. FIG. 1 shows a process diagram of the present invention.
原料大豆粉は、生大豆を脱皮、粉砕したものを用いる。
脱皮、粉砕を効率的に行なうために必要に応じて乾燥工
程を介在させるが、なお原料大豆粉には通常5〜8重量
%の水分が残存している。原料アルコールとして、最初
は純度95重量%以上のエタノール(水分5重量%以下
)を用いる。両者を混合、攪拌して均一なスラリー状態
とした後、容器を加温、減圧してエタノール分を蒸発さ
せる。容器として壁面を熱媒で加熱することのできる攪
拌機付密閉構造のものを使用し、バッチ式に上記処理を
行なうのが簡便確実であるが、連続式抽気乾燥機を用い
て連続処理することもできる。蒸発した蒸気は、凝縮器
に導きエタノールと水の大部分及び臭気成分の一部を凝
縮させる。臭気成分の残部を含む不凝縮性ガスは真空ポ
ンプの如き真空発生装置より排出し容器及び凝縮器の内
部圧力を減圧状態に維持する。エタノール分を蒸発除去
した大豆粉を容器より取出し、必要に応じて冷却、篩分
して製品とする。この製品の大豆粉は、実質的に臭気成
分が除去され、NSI値は原料大豆粉に比較して実質的
に低下していない。凝縮回収アルコールにはエタノール
、水、臭気成分を含むのでアルコール精製装置に送り、
水分と臭気成分を除去しエタノールの純度を向上させる
。The raw soybean flour is made by dehulling and crushing raw soybeans.
Although a drying step is performed as necessary to ensure efficient dehulling and pulverization, the raw soybean flour usually contains 5 to 8% by weight of water. As the raw alcohol, ethanol with a purity of 95% by weight or more (water content of 5% by weight or less) is initially used. After mixing and stirring the two to form a uniform slurry, the container is heated and depressurized to evaporate the ethanol content. It is simple and reliable to use a container with a sealed structure equipped with a stirrer whose walls can be heated with a heating medium and perform the above treatment in a batch manner, but it is also possible to carry out continuous treatment using a continuous extraction dryer. can. The evaporated vapor is directed to a condenser where most of the ethanol and water and some of the odor components are condensed. The non-condensable gas containing the remainder of the odor components is discharged from a vacuum generating device such as a vacuum pump to maintain the internal pressure of the container and condenser at a reduced pressure. The soybean flour from which the ethanol content has been evaporated is taken out from the container, cooled and sieved as needed to produce a product. In the soybean flour of this product, odor components have been substantially removed, and the NSI value is not substantially lower than that of the raw soybean flour. The condensed and recovered alcohol contains ethanol, water, and odor components, so it is sent to an alcohol purification equipment.
Improves the purity of ethanol by removing moisture and odor components.
第2図はアルコール精製装置の一例を示す。FIG. 2 shows an example of an alcohol purification apparatus.
蒸・留塔11の塔底12から、エタノールを実質的に含
有しない水分を取出し、塔頂13からは純度90%以上
のエタノール水溶液を取出す。臭気成分のうち高沸点成
分は、塔底12の水分とともに取出され、低沸点成分は
塔頂13から排出されるのて、塔頂蒸気を分縮して臭気
成分とエタノール、水共沸成分とを分離する。Water substantially free of ethanol is taken out from the bottom 12 of the distillation column 11, and an aqueous ethanol solution with a purity of 90% or more is taken out from the top 13. Among the odor components, the high boiling point components are taken out together with the water at the bottom 12 of the column, and the low boiling point components are discharged from the top 13 of the column. Separate.
14は凝縮液、15は冷却水用バイブ、16は不凝縮ガ
ス、17は真空ポンプ、18は精製アルコールタンク、
19は凝縮回収アルコール供給管、20は加熱蒸気用管
、21は廃水タンクである。14 is a condensate, 15 is a cooling water vibrator, 16 is a non-condensable gas, 17 is a vacuum pump, 18 is a purified alcohol tank,
19 is a condensed and recovered alcohol supply pipe, 20 is a heating steam pipe, and 21 is a waste water tank.
このようにして臭気成分含有量の少ない純度90%以上
のエタノール水溶液を精製アルコールとして回収するこ
とができる。そして精製アルコールを原料アルコールと
して再使用する。第4図は、本発明を実施する工程図を
示し、41はジャケット付攪拌乾燥機、42は減速機付
電動機、50は製品大豆粉ホッパー、44は凝縮器、4
8は凝縮回収アルコールタンク、11は蒸留塔、14は
凝縮器、21は廃水タンク、18は精製アルコールタン
クである。In this way, an aqueous ethanol solution with a purity of 90% or more and a low content of odor components can be recovered as purified alcohol. The purified alcohol is then reused as raw alcohol. FIG. 4 shows a process diagram for carrying out the present invention, in which 41 is a jacketed stirring dryer, 42 is an electric motor with a speed reducer, 50 is a product soybean flour hopper, 44 is a condenser, 4
8 is a condensation recovery alcohol tank, 11 is a distillation column, 14 is a condenser, 21 is a waste water tank, and 18 is a purified alcohol tank.
以下実施例を示す。Examples are shown below.
実施例1
原料大豆粉として米国産生大豆を脱皮、粉砕したものを
200y1原料アルコールとして純度99.5%以上の
エタノールを180cc用い、第3図に示す容量100
0ccのジャケット付二ーダー31と凝縮器34を主体
とした装置を用いて混合攪拌スラリー化、蒸発乾燥、凝
縮アルコール38の回収を行つた。Example 1 200y1 raw soybean powder was obtained by dehulling and pulverizing American soybeans, and 180cc of ethanol with a purity of 99.5% or higher was used as raw material alcohol, and the volume was 100ml as shown in Figure 3.
Mixing and stirring to form a slurry, evaporation drying, and recovery of condensed alcohol 38 were carried out using an apparatus mainly consisting of a 0 cc jacketed kneader 31 and a condenser 34.
下記の操作条件において得られた製品大豆粉は生ぐさい
臭気や苦味がなく、淡黄色、良質の粉末であつた。原料
大豆粉、製品大豆粉並びに、原料アルコール、凝縮回収
アルコールの品質数値を対比して示すと次表の通りであ
る。製品の大豆粉は蛋白質、脂質等有用成分の低下もな
く、また水溶性蛋白質、NS■値も高率で食品用として
優秀な特性を有していた。なお、30は蒸気用バイブ、
32は減速機付電動機、35は冷却水用管、37はアス
ビレータ、38は凝縮回収アルコールである。The product soybean flour obtained under the following operating conditions had no raw odor or bitter taste, had a pale yellow color, and was of good quality. The following table shows a comparison of the quality values of raw soybean flour, product soybean flour, raw alcohol, and condensed recovered alcohol. The product soybean flour had excellent properties for food use, with no decrease in useful components such as protein and lipids, and high percentages of water-soluble protein and NS* values. In addition, 30 is a steam vibrator,
32 is an electric motor with a speed reducer, 35 is a cooling water pipe, 37 is an asvilator, and 38 is a condensed recovery alcohol.
操作条件:
ニーダー内圧力、温度:10田)Rr,4O〜45凝縮
器冷却水温度:10℃蒸発開始より終点までの時間:4
紛
比較例1
実施例1において凝縮回収したアルコールを原料アルコ
ールとして繰返し使用し、原料大豆粉は毎回新しいもの
を使用して;8回目に得られた製品大豆粉と凝縮回収ア
ルコールの品質は次の通りであつた。Operating conditions: Kneader internal pressure, temperature: 10) Rr, 4O~45 Condenser cooling water temperature: 10°C Time from start of evaporation to end point: 4
Powder Comparison Example 1 The alcohol condensed and recovered in Example 1 was used repeatedly as the raw material alcohol, and the raw soybean powder was new each time; the quality of the product soybean flour and condensed recovered alcohol obtained in the 8th time was as follows. It was hot on the street.
実施例2
比較例1において得られた凝縮回収アルコールを直径3
0W!77!、段数27段のガラス製蒸留塔を主体とし
た第2図に示す蒸留装置を用いて精製し、水分9重量%
、エタノール分91重量%の精製アルコールを得た。Example 2 The condensed recovered alcohol obtained in Comparative Example 1 was
0W! 77! , purified using the distillation apparatus shown in Figure 2, mainly consisting of a glass distillation column with 27 plates, to a water content of 9% by weight.
, purified alcohol with an ethanol content of 91% by weight was obtained.
この精製アルコールを用いて実施例1に記載した方法で
原料大豆粉を処理し、臭気、苦味のない淡黄色、良質の
製品大豆粉を得た。製品大豆粉の分析値は水分3.6%
、蛋白質39.7%、水溶性蛋白質30.8%、NSI
値7.8%であつた。上記の実施例にみる通り、本発明
の方法によつてアルコールを用いて大豆蛋白のNSI値
を低下させることなく、臭気成分を除去した良質の製品
大豆粉を、産業規模において製造することができる。Raw soybean flour was treated with this purified alcohol in the manner described in Example 1 to obtain a product soybean flour of good quality and pale yellow with no odor or bitterness. The analysis value of the product soybean flour is 3.6% moisture.
, protein 39.7%, water soluble protein 30.8%, NSI
The value was 7.8%. As shown in the above examples, by the method of the present invention, high-quality product soybean flour from which odor components have been removed can be produced on an industrial scale without using alcohol to lower the NSI value of soybean protein. .
第1図、第2図、第3図及び第4図は、本発明を実施す
る工程図である。
11・・・・・・蒸留塔、14・・・・・凝縮器、18
・・・・・・精製アルコールタンク、1911−I凝縮
回収アルコール供給管、31・・・・・・ジャケット付
二ーダー、34・・・凝縮器、41・・・・・・ジャケ
ット付攪拌乾燥機、44・・・・・凝縮器、48・・・
・・凝縮回収アルコールタンク、50・・・・・・製品
大豆粉ホッパー。FIG. 1, FIG. 2, FIG. 3, and FIG. 4 are process diagrams for implementing the present invention. 11... Distillation column, 14... Condenser, 18
...Purified alcohol tank, 1911-I condensed and recovered alcohol supply pipe, 31 ... Jacketed seconder, 34 ... Condenser, 41 ... Jacketed stirring dryer , 44... condenser, 48...
... Condensate recovery alcohol tank, 50 ... Product soybean flour hopper.
Claims (1)
大豆粉を減圧乾燥させることにより、臭気成分を除去し
た大豆粉を得る一方、減圧により蒸発した水分及び臭気
成分を含有するアルコールを冷却凝縮し、凝縮液として
回収し、該凝縮液に含有される水分及び臭気成分を精製
して除去し、凝縮液のアルコール純分を高めた後、再使
用することを特徴とする臭気成分を除去した大豆粉の製
造方法。1. Soybean flour slurried with alcohol or alcohol aqueous solution is dried under reduced pressure to obtain soybean flour from which odor components have been removed, while water evaporated under reduced pressure and alcohol containing odor components are cooled and condensed and recovered as a condensate. A method for producing soybean flour from which odor components have been removed, characterized in that the water and odor components contained in the condensate are purified and removed, the alcohol purity of the condensate is increased, and then the condensate is reused.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53040912A JPS6057822B2 (en) | 1978-04-07 | 1978-04-07 | Method for producing soybean flour from which odor components have been removed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53040912A JPS6057822B2 (en) | 1978-04-07 | 1978-04-07 | Method for producing soybean flour from which odor components have been removed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54135250A JPS54135250A (en) | 1979-10-20 |
| JPS6057822B2 true JPS6057822B2 (en) | 1985-12-17 |
Family
ID=12593704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53040912A Expired JPS6057822B2 (en) | 1978-04-07 | 1978-04-07 | Method for producing soybean flour from which odor components have been removed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6057822B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020058245A (en) * | 2018-10-05 | 2020-04-16 | 学校法人関東学院 | Soy flour production method, soy flour produced by the production method, and soybean processed food containing the soy flour |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58162253A (en) * | 1982-03-19 | 1983-09-26 | Ajinomoto Co Inc | Preparation of soybean milk |
| US4450176A (en) * | 1982-08-23 | 1984-05-22 | Land O'lakes, Inc. | Method of treating soybean material |
-
1978
- 1978-04-07 JP JP53040912A patent/JPS6057822B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020058245A (en) * | 2018-10-05 | 2020-04-16 | 学校法人関東学院 | Soy flour production method, soy flour produced by the production method, and soybean processed food containing the soy flour |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54135250A (en) | 1979-10-20 |
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