JPH0448417B2 - - Google Patents

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Publication number
JPH0448417B2
JPH0448417B2 JP61040986A JP4098686A JPH0448417B2 JP H0448417 B2 JPH0448417 B2 JP H0448417B2 JP 61040986 A JP61040986 A JP 61040986A JP 4098686 A JP4098686 A JP 4098686A JP H0448417 B2 JPH0448417 B2 JP H0448417B2
Authority
JP
Japan
Prior art keywords
soybeans
soybean
split
temperature
peeling
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 - Lifetime
Application number
JP61040986A
Other languages
Japanese (ja)
Other versions
JPS62198364A (en
Inventor
Masahiko Samoto
Susumu Teranishi
Shuichi Okada
Kazuto Majima
Masahiko Terajima
Seizo Taniguchi
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.)
Fuji Oil Co Ltd (fka Fuji Oil Holdings Inc)
Original Assignee
Fuji Oil 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 Fuji Oil Co Ltd filed Critical Fuji Oil Co Ltd
Priority to JP61040986A priority Critical patent/JPS62198364A/en
Publication of JPS62198364A publication Critical patent/JPS62198364A/en
Publication of JPH0448417B2 publication Critical patent/JPH0448417B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は大豆処理方法に関する。更に詳しく
は、風味及び色調が改良され、高いNSI(蛋白の
水溶性指標)を有する大豆子葉を提供するもので
あり、分離大豆蛋白、多糖類、少糖類、豆乳、組
織状若しくは繊維状等の蛋白食品の原料素材とし
て優れる大豆子葉を提供するものである。 (従来技術) 従来から豆腐等の原料として大豆を剥皮する方
法が多く知られている。なかでも、大豆を加熱し
て剥皮する方法としては、例えば、特開昭56−
84644、58−71858、59−147647、59−150550、59
−150661等を挙げることができる。 本発明と従来技術の主な違いは、本発明が大豆
を選別し、加熱乾燥し、二つ割れし、剥皮し、篩
別して大豆子葉を得る工程において大豆の水分を
12%以下に調整し、大豆の品温が70〜80℃となる
ようにして大豆の表面を均一に加熱乾燥し、脱
皮・脱胚軸を容易にし、微粉(グリツプ)発生量
が少なく、高NSIを保持する大豆子葉を高収率で
得ることにある。 (発明が解決しようとする問題点) 大豆は皮、胚軸、子葉からなり、皮には埃等が
付着し大豆製品(大豆を用いて得られる製品)の
色調や風味を悪化させる。又、胚軸はサポニンや
ポリフエノール化合物を多く含み大豆製品の風味
を悪化させる。そこで、本発明者等はこれら大豆
皮や大豆胚軸を除去し、風味・色調の改良された
高NSIを保持する大豆子葉を得ることを目的とし
た。 前記目的に沿つて、大豆を二つ割れさせ、脱
皮、脱胚軸を試みた。しかし、(a)二つ割れ・除皮
が困難であり、(b)二つ割れに伴う微粉砕部(グリ
ツツ)が生じ易く、(c)胚軸と子葉分離が困難であ
り、又、(d)大豆子葉蛋白のNSIを高く保つ脱皮・
脱胚軸条件の設定が困難である問題に遭遇した。 (問題を解決する為の手段) かかる目的を達成すべく原料大豆を選別し、グ
ラインダー等の二つ割れ手段を用いて二つ割れ
し、風選・除皮し、篩別して大豆子葉を得る条件
について種々検討するなかで、通常12〜15%程度
の水分を含む大豆を、予め大豆水分を12%以下
に調整しておいて、大豆の品温(大豆を温度計
で測定した実測温度)が70〜80℃となるように比
較的短時間で均一加熱すれば、大豆の表面部分を
均一に乾燥でき、且つ大豆の内部は大豆が柔らか
さを保つ温度に昇温でき、(a)二つ割れ・除皮が容
易に出来、(b)二つ割れ・篩別しても微粉砕部(グ
リツツ)が生じ難く、(c)胚軸と子葉分離が容易に
でき、(d)二つ割れ・篩別された若干の皮を有する
大豆子葉部を剥皮手段を用いて除皮するすること
が容易にでき、(e)かかる(除皮されて)脱皮・脱
胚軸された大豆子葉蛋白のNSIを高く保つことが
できる知見を得て本発明を完成するに到つた。 即ち、本発明は、大豆の水分を12%以下に調整
し、大豆の品温が70〜80℃となるように加熱乾燥
し、二つ割れする工程と二つ割れされた大豆を剥
皮する工程を組合せて大豆子葉を得ることを特徴
とする大豆処理方法である。 本発明に用いる大豆は、公知の大豆を用いるこ
とができる。通常、原料大豆は未熟豆、夾雑物等
を含む為、選別し粒度を揃えるほうが後の処理を
容易にし好ましい。選別の方法は、篩選別、ロー
ル選別、風選別、密度選別等の公知の選別手段を
利用することができる。 本発明は、大豆の水分を12%以下に調整する工
程と、大豆の品温が70〜80℃になるように加熱乾
燥する工程と、乾燥された大豆を二つ割れし、二
つ割れされた大豆(皮を若干含む場合)を剥皮す
る工程を組み合わせることに特徴を有する。かか
る組合せにより目的を達成することができる。 まず、大豆の水分を12%以下(好適には8〜12
%、更に好適には10〜11%)に調整することが好
ましい。通常大豆は12〜15%の水分を含んでいる
ので低温(通常60〜70℃)でゆつくり乾燥して大
豆水分が12%以下になるように調整することがで
きる。獲られる子葉を圧扁して大豆油抽出に供す
るには8〜12%の水分が圧扁子葉を獲るのに好適
である。大豆水分が8%以下では得られる大豆子
葉を圧扁する際、砕けやすく好ましくない。既に
かかる水分範囲にある大豆は水分調整の必要はな
い。又、大豆水分が8%未満の大豆は過加湿する
等して水分が8〜12%になるように調整するほう
が好ましい。又、大豆水分が12%を越えると二つ
割れ・除皮がうまく行えず好ましくない。大豆水
分を12%以下に調整する手段は公知の乾燥手段を
用いることができる。例えば、通気竪型乾燥機、
向流多段式乾燥機、通気回転乾燥機等。乾燥温度
は比較的低く(通常60〜70℃程度)、乾燥時間は
比較的遅い(通常30〜60分程度)ほうが好ましい
傾向にある。 次ぎに、水分12%以下に調整された大豆を、大
豆の品温が70〜80℃となるように乾燥することが
重要である。大豆の品温は70℃未満では、大豆の
加熱乾燥と柔軟性が十分ではなく、次の二つ割れ
工程においてグリツツの発生が多くなり大豆子葉
の収率が悪化し好ましくない。又、大豆の品温が
80℃を越えると、得られた大豆子葉のNSIが低下
するので好ましくない。品温が70〜80℃の大豆は
二つ割れするに適度の柔軟性を有し、グリツツの
発生を少なく破砕でき、除皮を容易にし、且つ
NSIの低下をきたすことができなく好適である。
大豆が70〜80℃加熱で適度の柔軟性を保持する水
分範囲は約7〜11%を目安とすることができる。
余り乾燥し過ぎると大豆の加熱状態における柔軟
性が失われ二つ割れ工程におけるグリツツの発生
を増大させる傾向にある。 かかる大豆内部が適度の柔軟性を保持し、大豆
の表面を均一に乾燥するのに適した乾燥手段は、
例えば、流動層乾燥、エアーベツド、ロータリー
キルン等を利用することができ。なかでも流動層
乾燥は均一な大豆表面乾燥に適し最も好適であ
る。 例えば、流動層乾燥の条件は、通常熱風温度80
℃〜90℃、層内温度75℃〜85℃、滞留時間3〜4
分程度が好適であり、スケール、目的により適宜
条件を変化させることができる。 次ぎに、乾燥処理し適度の内部柔軟性と表面の
脆性を有する大豆を二つ割れする。二つ割れは公
知の粗砕機(例えば、グラインダー、ゴムロー
ル、クラツキングロール等)を用いることができ
る。例えば、グラインダーを用いる場合、大豆粒
径よりやや広い砥石間間隔のグラインダーを用い
ることが好ましい。大豆粒径より狭い砥石間間隔
のグラインダーを用いるとうまく二つ割れになれ
ずグリツツの発生が増大し子葉の収率が悪化す
る。又、砥石間間隔が広すぎると、未割れ大豆量
が多くなり好ましくない。 例えば、粒径6.5mmφの大豆を二つ割れすると
きの砥石間間隔は7mm程度が適当である。 二つ割れの際、大豆の品温が下がらないように
するほうが好ましく、若し下がる場合でも50℃以
上が好ましい。品温が下がると大豆が硬くなり二
つ割れによりグリツツの発生が多くなる傾向にあ
る。 一度品温が下がると大豆は硬くなり、二つ割
れ・除皮が困難になる傾向にあるので、もういち
ど加熱したほうが好ましい。 又、グラインダーを用いる場合、砥石の回転数
は比較的遅いほうがグリツツの発生が少なくなる
傾向にある。 尚、二つ割れされた大豆は、風選して除皮し、
篩別して得られる未二つ割れ大豆(通常、1話程
度発生することが多い、発生しない場合は再二つ
割れする必要はない)を再度二つ割れすることを
繰り返すことができる。通常再二つ割れ処理で完
全に二つ割れにすることができる。二つ割れは前
述の大豆の二つ割れと同様にすることができる。
例えば、グラインダイーを用いる場合は、未二つ
割れ大豆の粒径は通常約5mm程度となるので、グ
ラインダーの砥石間間隔は5.5mm程度が好ましい。
尚、再度二つ割れする場合は、未二つ割れ大豆を
別段加熱乾燥処理する必要はない。 二つ割れした大豆は、所望により風選して除皮
し、篩別して胚軸部やグリツツを除去し、大豆子
葉部を得ることができる。通常、かかる二つ割れ
し、篩別した大豆子葉部は未だ20%(対大豆全体
の皮)程度の皮が付着している場合が多いので、
かかる篩別した大豆子葉部を40℃以下(好ましく
は30℃以下)に冷却後、剥皮手段を用いて剥皮し
除去するほうが好ましい。剥皮手段は、グライン
ダー、剥皮機、手揉み等の公知の手段を用いるこ
とができる。グラインダーを用いる場合、砥石間
間隔は二つ割れされた大豆粒子径より広いほうが
好ましい。 前記皮を含む大豆子葉部は、冷却するほど剥皮
手段による剥皮効果が増大する傾向にあり、30℃
以下になると剥皮効果は略平衡に達する。例えば
60℃から30℃までは剥皮率(大豆全体の皮に対す
る剥皮された皮の重量割合)は8%程度比較的に
増加する傾向にある。 尚、冷却の手段は放置冷却、強制冷却(例え
ば、振動通風冷却機、回転通風冷却機等の機械的
手段等)等の公知の手段を用いることができる。 以上のように、二つ割れされ、剥皮されて脱
皮・脱胚軸されて得られる大豆子葉部は皮、胚軸
を殆ど含まず目的に合致した大豆子葉とすること
ができる。 尚、前記二つ割れ後の除皮や剥皮後の除皮は、
公知の手段(例えば、アスピレーター、風力分級
機等)を用いることができる。 又、前記二つ割れ後の篩別は公知の篩別機(例
えば、ロータリーシフター、振動篩等)を用いる
ことができる。 以上の工程で獲られる子葉部は、収率が高く
(通常約85%以上対大豆、95%以上対大豆の子葉
部)で、風味及び色調の改良され、且つ変性の程
度が極めて低いのでNSIが高く(通常NSIの低下
は約2%未満)、分離大豆蛋白、多糖類、少糖類、
豆乳、組織状若しくは繊維状等の蛋白食品の原料
素材として優れるものである。 (実施例) 以下実施例により本発明の実施態様を説明す
る。 実施例 1 アメリカ産大豆(水分12%)を、4.8×12mmの
網目を有する篩を用いて選別し、平均粒径6.6mm
φ(粒径5.4〜8.4mmφ)の大豆を得た。 選別大豆を予備乾燥(70℃の熱風にて30分間)
して水分を11%に調整した。 水分11%の大豆5000重量部(以下 部)を、実
験用流動層乾燥装置を用いて、熱風風速3.4m/
secにて、表−1に示す条件にて加熱乾燥処理し、
ただちに豆腐製造用グラインダー(栗原鉄工(株)
製)を用い、砥石間間隔7mmにて二つ割れし、風
力分級機(風速3〜5m/sec)にて除皮(288
部)し、4.3×19mmの篩を用いて未二つ割れ大豆
(500部)を篩別・分取し、これを砥石間間隔5.5
mmのグラインダーで再二つ割れし、同様に除皮
(39部)して二つ割れ大豆を獲た。 二つ割れ大豆を、8メツシユ篩を用いて、子葉
部(4422部)及び胚軸部とグリツツ部(合計250
部)に篩別した。 子葉部をアスピレーターを用いて30℃まで冷却
し、再度グラインダー(砥石間間隔7mm)に通
し、風選、篩別して皮部(66部)とグリツツ部
(24部)を除去して子葉部4324部を獲た。 大豆の除皮率、脱胚軸率、得られた子葉部の
NSIを表−1に合わせ示す。
(Industrial Application Field) The present invention relates to a soybean processing method. More specifically, it provides soybean cotyledons with improved flavor and color tone and high NSI (protein water solubility index), including isolated soybean protein, polysaccharides, oligosaccharides, soybean milk, textured or fibrous, etc. The present invention provides soybean cotyledons that are excellent as raw materials for protein foods. (Prior Art) Many methods have been known for peeling soybeans as raw materials for tofu and the like. Among them, methods for heating and peeling soybeans include, for example,
84644, 58−71858, 59−147647, 59−150550, 59
-150661 etc. The main difference between the present invention and the prior art is that the present invention removes moisture from soybeans in the process of sorting, heating drying, splitting them into two, peeling, and sieving to obtain soybean cotyledons.
The surface of the soybeans is evenly heated and dried by adjusting the soybean temperature to 70 to 80℃, making it easier to molt and remove the hypocotyls, generate less fine powder (grips), and increase the The aim is to obtain high yields of soybean cotyledons that retain NSI. (Problems to be Solved by the Invention) Soybeans are composed of skin, hypocotyls, and cotyledons, and dust and the like adhere to the skin, which deteriorates the color tone and flavor of soybean products (products obtained using soybeans). In addition, the hypocotyl contains a large amount of saponin and polyphenol compounds, which deteriorate the flavor of soybean products. Therefore, the present inventors aimed to remove these soybean hulls and soybean hypocotyls to obtain soybean cotyledons that have improved flavor and color and retain high NSI. In line with the above purpose, soybeans were split into two, and attempts were made to molt the soybean and remove the hypocotyl. However, (a) it is difficult to split into two and remove the skin, (b) finely pulverized parts (grits) are likely to occur due to splitting, (c) it is difficult to separate the hypocotyl and cotyledons, and ( d) Dehulling to keep the NSI of soybean cotyledon protein high
I encountered a problem in which it was difficult to set the conditions for removing hypocotyl. (Means for solving the problem) Conditions for obtaining soybean cotyledons by sorting raw soybeans, splitting them into two using a splitting means such as a grinder, wind-selecting, removing the skin, and sieving to achieve the above purpose. While conducting various studies, we found that soybeans, which normally have a moisture content of about 12 to 15%, were adjusted in advance to below 12% moisture, and the temperature of the soybeans (actual temperature measured using a soybean thermometer) was By uniformly heating the soybeans in a relatively short period of time to 70-80℃, the surface of the soybeans can be dried uniformly, and the inside of the soybeans can be heated to a temperature at which the soybeans remain soft. It can be easily cracked and peeled, (b) finely pulverized parts (grits) are not easily generated even when split in two and sieved, (c) hypocotyls and cotyledons can be easily separated, and (d) split in half and sieved. The separated soybean cotyledon having some skin can be easily removed using a peeling means, and (e) the NSI of the soybean cotyledon protein that has been peeled off and dehulled and hypocotyl can be obtained. The present invention was completed based on the knowledge that it is possible to maintain a high temperature. That is, the present invention includes a process of adjusting the moisture content of soybeans to 12% or less, heating and drying the soybeans to a temperature of 70 to 80°C, and splitting the soybeans into two, and a process of peeling the split soybeans. This is a soybean processing method characterized by obtaining soybean cotyledons by combining the following. Known soybeans can be used as the soybeans used in the present invention. Normally, raw soybeans contain immature beans, impurities, etc., so it is preferable to sort them to make the particle size uniform, as this makes subsequent processing easier. As a method of sorting, known sorting means such as sieve sorting, roll sorting, wind sorting, density sorting, etc. can be used. The present invention involves a process of adjusting the moisture content of soybeans to 12% or less, a process of heating and drying the soybeans to a temperature of 70 to 80℃, and splitting the dried soybeans into two. It is characterized by combining the process of peeling the soybeans (if they contain some skin). The purpose can be achieved by such a combination. First, reduce the moisture content of soybeans to 12% or less (preferably 8 to 12%).
%, more preferably 10 to 11%). Normally, soybeans contain 12 to 15% moisture, so by slowly drying them at low temperatures (usually 60 to 70°C), the moisture content of soybeans can be adjusted to below 12%. A moisture content of 8 to 12% is suitable for compressing the harvested cotyledons to extract soybean oil. When the soybean moisture content is less than 8%, the resulting soybean cotyledons tend to crumble when pressed, which is not preferable. Soybeans already within this moisture range do not require moisture adjustment. In addition, it is preferable to adjust the moisture content of soybeans with a moisture content of less than 8% to 8 to 12% by over-humidifying the soybeans. Also, if the moisture content of soybeans exceeds 12%, splitting and peeling of the soybeans cannot be performed properly, which is undesirable. A known drying method can be used to adjust the soybean moisture content to 12% or less. For example, a ventilated vertical dryer,
Countercurrent multistage dryer, ventilation rotary dryer, etc. It tends to be preferable for the drying temperature to be relatively low (usually about 60 to 70°C) and the drying time to be relatively slow (usually about 30 to 60 minutes). Next, it is important to dry the soybeans whose moisture content has been adjusted to 12% or less so that the soybean temperature is 70 to 80°C. If the temperature of the soybean is less than 70°C, the heat drying and flexibility of the soybean will not be sufficient, and the generation of grits will increase in the next halving process, which will deteriorate the yield of soybean cotyledons, which is undesirable. Also, the temperature of soybeans
If the temperature exceeds 80°C, the NSI of the obtained soybean cotyledons decreases, which is not preferable. Soybeans with a temperature of 70 to 80°C have the appropriate flexibility to be broken into two, can be crushed with less grit, and can be easily removed.
This is suitable because it does not cause a decrease in NSI.
The moisture range in which soybeans maintain appropriate flexibility when heated to 70 to 80°C can be set at approximately 7 to 11%.
If the soybean is too dry, it tends to lose its flexibility when heated and increase the occurrence of grits during the halving process. Drying means suitable for maintaining the appropriate flexibility inside the soybean and uniformly drying the surface of the soybean include:
For example, fluidized bed drying, airbed drying, rotary kiln, etc. can be used. Among them, fluidized bed drying is the most suitable because it is suitable for uniform surface drying of soybeans. For example, the conditions for fluidized bed drying are usually a hot air temperature of 80°C.
°C to 90 °C, temperature inside the bed 75 °C to 85 °C, residence time 3 to 4
Approximately a minute is suitable, and the conditions can be changed as appropriate depending on the scale and purpose. Next, the soybeans that have been dried and have appropriate internal flexibility and surface brittleness are split into two. A known coarse crusher (for example, a grinder, a rubber roll, a cracking roll, etc.) can be used to divide the mixture into two. For example, when using a grinder, it is preferable to use a grinder with a grindstone spacing slightly wider than the soybean grain size. If a grinder with a grinding wheel spacing narrower than the soybean grain size is used, the soybean cannot be split into two properly, resulting in increased occurrence of grits and poor cotyledon yield. Moreover, if the distance between the grinding wheels is too wide, the amount of unbroken soybeans will increase, which is not preferable. For example, when splitting soybeans with a grain size of 6.5 mmφ into two, the appropriate distance between grinding wheels is about 7 mm. When splitting into two, it is preferable to prevent the temperature of the soybeans from dropping, and even if it does, it is preferably 50°C or higher. As the temperature drops, soybeans become harder and tend to crack into two, causing more grit. Once the temperature drops, soybeans tend to become hard and difficult to split in half and remove the skin, so it is better to heat them again. Further, when using a grinder, the generation of grit tends to be reduced when the rotation speed of the grindstone is relatively low. In addition, the soybeans that have been split into two are wind-selected and the skins are removed.
It is possible to repeatedly split the un-halved soybeans obtained by sieving (usually, about one episode occurs; if this does not occur, there is no need to split the soybeans into two again). Normally, it can be completely split into two by re-splitting process. Breaking into two can be done in the same way as the above-mentioned splitting of soybeans into two.
For example, when using a grinder, the grain size of unsplit soybeans is usually about 5 mm, so the distance between the grinding wheels of the grinder is preferably about 5.5 mm.
In addition, if the soybeans are to be split into two again, there is no need to separately heat and dry the unbroken soybeans. The soybean split in two can be wind-selected to remove the skin, if desired, and sieved to remove the hypocotyl and grits to obtain the soybean cotyledon. Normally, the soybean cotyledons that have been split into two and sieved often still have about 20% of the skin attached (based on the skin of the whole soybean).
It is preferable to cool the sieved soybean cotyledon to 40° C. or below (preferably 30° C. or below) and then peel and remove the skin using a peeling means. As the peeling means, known means such as a grinder, a peeling machine, and hand kneading can be used. When using a grinder, it is preferable that the distance between the grinding wheels be wider than the diameter of the soybean particles split into two. The peeling effect of the peeling means tends to increase as the soybean cotyledon containing the skin is cooled;
Below that, the peeling effect reaches approximately equilibrium. for example
From 60°C to 30°C, the peeling rate (weight ratio of peeled skin to whole soybean skin) tends to increase by about 8%. Note that known means such as left cooling, forced cooling (for example, mechanical means such as an oscillating draft cooler and a rotary draft cooler) can be used as the cooling means. As described above, the soybean cotyledon obtained by splitting the soybean into two, peeling, and dehulling/dehulling the hypocotyl contains almost no skin or hypocotyl, and can be used as a soybean cotyledon that meets the purpose. In addition, the skin removal after splitting in two and the skin removal after peeling are as follows:
Known means (eg, aspirator, wind classifier, etc.) can be used. In addition, a known sieving machine (for example, a rotary shifter, a vibrating sieve, etc.) can be used for sieving after the above-mentioned halving. The cotyledon obtained through the above process has a high yield (usually about 85% or more for soybean, 95% or more for soybean cotyledon), has improved flavor and color, and has an extremely low degree of denaturation, so it is NSI (usually less than about 2% decrease in NSI), isolated soy protein, polysaccharides, oligosaccharides,
It is excellent as a raw material for protein foods such as soy milk, textured or fibrous protein foods. (Example) Embodiments of the present invention will be described below with reference to Examples. Example 1 American soybeans (moisture 12%) were sorted using a sieve with a mesh size of 4.8 x 12 mm, and the average particle size was 6.6 mm.
Soybeans of φ (particle size 5.4 to 8.4 mmφ) were obtained. Pre-drying the sorted soybeans (30 minutes with hot air at 70℃)
The moisture content was adjusted to 11%. 5000 parts by weight (hereinafter referred to as "parts") of soybeans with a moisture content of 11% were heated with hot air at a speed of 3.4 m/cm using an experimental fluidized bed dryer.
sec, heated and dried under the conditions shown in Table 1,
Grinder for immediate tofu production (Kurihara Iron Works Co., Ltd.)
It was divided into two pieces with a grindstone spacing of 7 mm using a grinding wheel (manufactured by J.D. Co., Ltd.), and the skin was removed using a wind classifier (wind speed of 3 to 5 m/sec).
part), use a 4.3 x 19 mm sieve to sieve and separate the unhalved soybeans (500 parts), and separate the soybeans with a grinding wheel spacing of 5.5 mm.
The soybeans were split into two again using a mm grinder, and the skin was removed in the same way (39 parts) to obtain split soybeans. Split soybeans were separated into cotyledons (4422 parts), hypocotyl parts and grit parts (total 250 parts) using an 8-mesh sieve.
). The cotyledon part was cooled to 30℃ using an aspirator, passed through the grinder again (7 mm distance between grinding wheels), screened and sieved to remove the skin part (66 parts) and grit part (24 parts), resulting in 4324 parts of the cotyledon part. won. Dehulling rate of soybean, hypocotyl removal rate, and obtained cotyledon part
NSI is shown in Table-1.

【表】 但し、(A)は加熱乾燥温度(加熱時間は3分とし
た)、(B)は大豆品温、(C)は大豆除皮率※1、(D)は
脱胚軸率※2、(E)はNSI※2を表す。 又、※1:大豆除皮率(%)=100×(製品中の
残存大豆皮の重量)/(選別大豆の重量×0.08)
(大豆皮の割合を8%として計算した。) ※2:脱胚軸率(%)=100×(製品中の残存大
豆皮胚軸の重量)/(選別大豆の重量×0.025)
(大豆胚軸の割合を2.5%として計算した。) ※3:NSIは全蛋白に対する水溶性蛋白の割合
(%)であり、公知の測定法によつた。 応用例 1 実施例1のNo.5と同様にして得た子葉部4000重
量部を圧扁し、n−ヘキサン(10倍)抽出を二回
行つて風乾し、脱脂子葉(残油分約0.5%)を調
整した。この脱脂子葉に10倍量の水を加えて40℃
で40分間撹拌・抽出し、オカラを除いて得た豆乳
を塩酸を用いて等電沈澱(PH4.5)させ、得られ
たカードを苛性ソーダを用いて中和し、10%溶液
としたものをUHT式高温瞬間殺菌(135℃で10
秒)し、スプレー乾燥して分離大豆蛋白を得た。 比較例 1 大豆を実施例1と同様に処理して脱脂大豆を調
整し、実施例1の同様に処理して分離大豆蛋白を
得た。 実験例 1 実施例1で得られた分離大豆蛋白と、比較例1
で得られた分離大豆蛋白とを各々10%溶液とな
し、10名のパネラーにより風味等の検査を行つ
た。結果を表−2に示す。
[Table] However, (A) is the heating drying temperature (heating time was 3 minutes), (B) is the soybean product temperature, (C) is the soybean dehulling rate *1, and (D) is the hypocotyl removal rate * 2. (E) represents NSI*2. Also, *1: Soybean hull removal rate (%) = 100 x (weight of remaining soybean hulls in the product) / (weight of sorted soybeans x 0.08)
(Calculated assuming the percentage of soybean hulls is 8%.) *2: De-hypocotyl rate (%) = 100 x (weight of residual soybean hull hypocotyl in product) / (weight of sorted soybeans x 0.025)
(The ratio of soybean hypocotyl was calculated as 2.5%.) *3: NSI is the ratio (%) of water-soluble protein to total protein, and was determined by a known measurement method. Application example 1 4000 parts by weight of the cotyledon obtained in the same manner as No. 5 of Example 1 was pressed, extracted twice with n-hexane (10 times) and air-dried to obtain a defatted cotyledon (residual oil content of approximately 0.5%). ) was adjusted. Add 10 times the amount of water to this defatted cotyledon and heat at 40°C.
After stirring and extracting the soymilk for 40 minutes and removing okara, the obtained soymilk was subjected to isoelectric precipitation (PH4.5) using hydrochloric acid, and the resulting curd was neutralized using caustic soda to make a 10% solution. UHT type high temperature instant sterilization (10 at 135℃
) and spray dried to obtain isolated soybean protein. Comparative Example 1 Soybeans were treated in the same manner as in Example 1 to prepare defatted soybeans, and in the same manner as in Example 1, isolated soybean protein was obtained. Experimental Example 1 Isolated soybean protein obtained in Example 1 and Comparative Example 1
A 10% solution of each of the isolated soybean proteins obtained in the above was prepared, and a panel of 10 people tested the flavor, etc. The results are shown in Table-2.

【表】 但し、Aは実施例1の分離大豆蛋白、Bは比較
例1の分離大豆蛋白である。 応用例 2 応用例1と同様にして得た脱脂子葉に20重量%
の加水を行い、実験用2軸押出機を用い、スクリ
ユー回転数570R.P.M.、バレル温度170℃にて、
ダイ(5mmφ)より押し出して、繊維状構造に優
れた組織状蛋白を得た。 次ぎに、比較例1で用いた脱脂大豆を同様に処
理して繊維状構造に優れた組織状蛋白を得た。 得られた各々の組織状蛋白を湯戻し、水切り後
10名のパネラーにより風味等の検査を行つた。結
果を表−3に示す。
[Table] However, A is the isolated soybean protein of Example 1, and B is the isolated soybean protein of Comparative Example 1. Application example 2 20% by weight of defatted cotyledons obtained in the same manner as application example 1
using an experimental twin-screw extruder at a screw rotation speed of 570 R.PM and a barrel temperature of 170°C.
It was extruded through a die (5 mmφ) to obtain a textured protein with an excellent fibrous structure. Next, the defatted soybean used in Comparative Example 1 was treated in the same manner to obtain a textured protein with an excellent fibrous structure. After soaking each obtained tissue protein in hot water and draining the water,
Flavor etc. were tested by 10 panelists. The results are shown in Table-3.

【表】 但し、Aは脱脂大豆子葉の組織状蛋白、Bは脱
脂大豆の組織状蛋白である。 (効果) 以上、詳述したように、本発明により風味及び
色調の改良され、且つ高NSIを有する大豆子葉を
高収率で得ることが可能になつたものである。更
に、分離大豆蛋白、多糖類、少糖類、豆乳、組織
状若しくは繊維状等の蛋白食品の原料素材として
も優れる大豆子葉を、(a)大豆の二つ割れ・剥皮を
容易に、(b)微粉砕部(グリツツ)が生じ難く、(c)
胚軸と子葉分離を容易にする脱皮・脱胚軸方法を
可能にしたものである。尚、一般に大豆脱皮は大
豆のエージングによる効果があるが、本発明は別
段エージングを行う必要はない。 以上説明したように本発明は産業の発達に寄与
するところ大なるものである。
[Table] However, A is the textured protein of defatted soybean cotyledons, and B is the textured protein of defatted soybean. (Effects) As detailed above, the present invention makes it possible to obtain soybean cotyledons with improved flavor and color tone and high NSI at a high yield. Furthermore, soybean cotyledons, which are excellent raw materials for protein foods such as isolated soybean protein, polysaccharides, oligosaccharides, soymilk, and textured or fibrous products, can be used to (a) easily split and peel soybeans; (b) Finely pulverized parts (grits) are difficult to form, (c)
This enables a method of molting and removing hypocotyl that facilitates the separation of hypocotyls and cotyledons. Although soybean dehulling is generally effective by aging the soybean, the present invention does not require any special aging. As explained above, the present invention greatly contributes to the development of industry.

Claims (1)

【特許請求の範囲】 1 大豆の水分を12%以下に調整し、大豆の品温
が70〜80℃となるように加熱乾燥し、二つ割れす
る工程と二つ割れされた大豆を剥皮する工程を組
合せて大豆子葉を得ることを特徴とする大豆処理
方法。 2 二つ割れする態様が、品温が70〜80℃となる
ように乾燥した大豆を、大豆粒径より広い砥石間
間隔のグラインダーにかける特許請求の範囲第1
項記載の大豆処理方法。 3 剥皮する態様が、二つ割れされた大豆を30℃
以下に冷却後、剥皮手段を用いて剥皮する特許請
求の範囲第1項又は2項記載の大豆処理方法。 4 二つ割れする態様が、二つ割れし、篩別され
た未剥皮大豆を再度二つ割れする特許請求の範囲
第1項記載の大豆処理方法。
[Claims] 1. Adjusting the moisture content of soybeans to 12% or less, heating and drying the soybeans to a temperature of 70 to 80°C, and splitting the soybeans into two, and peeling the split soybeans. A soybean processing method characterized by obtaining soybean cotyledons by combining steps. 2. The aspect of splitting into two is that soybeans that have been dried to a temperature of 70 to 80°C are put through a grinder with a grindstone spacing wider than the soybean grain size.
Soybean processing method described in section. 3 The method of peeling is to cut the soybeans into two at 30°C.
The method for treating soybeans according to claim 1 or 2, wherein the soybean is cooled and then peeled using a peeling means. 4. The soybean processing method according to claim 1, in which the unhulled soybean that has been split into two and sieved is split into two again.
JP61040986A 1986-02-25 1986-02-25 Processing of soybean Granted JPS62198364A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61040986A JPS62198364A (en) 1986-02-25 1986-02-25 Processing of soybean

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61040986A JPS62198364A (en) 1986-02-25 1986-02-25 Processing of soybean

Publications (2)

Publication Number Publication Date
JPS62198364A JPS62198364A (en) 1987-09-02
JPH0448417B2 true JPH0448417B2 (en) 1992-08-06

Family

ID=12595747

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61040986A Granted JPS62198364A (en) 1986-02-25 1986-02-25 Processing of soybean

Country Status (1)

Country Link
JP (1) JPS62198364A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1099037A (en) * 1996-09-30 1998-04-21 Fuji Oil Co Ltd How to make soy food ingredients
CN101228922A (en) * 2007-01-26 2008-07-30 上海英颁斯物流科技有限公司 Method and device for cooling and peeling beans and corns
WO2010063057A1 (en) * 2008-12-05 2010-06-10 Grain Foods Crd Ltd An improved manufacturing process for a food product
JP6566381B2 (en) * 2015-06-02 2019-08-28 株式会社サタケ Legume preparation and shipping equipment
JP6639836B2 (en) * 2015-09-02 2020-02-05 日清オイリオグループ株式会社 Method for producing soybean oil, method for producing soybean tocopherol

Also Published As

Publication number Publication date
JPS62198364A (en) 1987-09-02

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