JPH04112763A - Preparation of defatted soybean and tissue-like soybean protein - Google Patents
Preparation of defatted soybean and tissue-like soybean proteinInfo
- Publication number
- JPH04112763A JPH04112763A JP2232829A JP23282990A JPH04112763A JP H04112763 A JPH04112763 A JP H04112763A JP 2232829 A JP2232829 A JP 2232829A JP 23282990 A JP23282990 A JP 23282990A JP H04112763 A JPH04112763 A JP H04112763A
- Authority
- JP
- Japan
- Prior art keywords
- soybean
- soybeans
- heating
- defatted
- live steam
- 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.)
- Pending
Links
- 235000010469 Glycine max Nutrition 0.000 title claims abstract description 68
- 244000068988 Glycine max Species 0.000 title claims abstract description 67
- 108010073771 Soybean Proteins Proteins 0.000 title description 8
- 235000019710 soybean protein Nutrition 0.000 title description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 28
- 238000007664 blowing Methods 0.000 claims abstract description 11
- 238000007796 conventional method Methods 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 3
- 238000010793 Steam injection (oil industry) Methods 0.000 claims 1
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 235000020985 whole grains Nutrition 0.000 claims 1
- 239000000796 flavoring agent Substances 0.000 abstract description 16
- 235000019634 flavors Nutrition 0.000 abstract description 16
- 238000001035 drying Methods 0.000 abstract description 6
- 238000003825 pressing Methods 0.000 abstract description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 9
- 230000000694 effects Effects 0.000 description 6
- 239000003921 oil Substances 0.000 description 4
- 235000019198 oils Nutrition 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000001877 deodorizing effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 210000000988 bone and bone Anatomy 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
Landscapes
- Beans For Foods Or Fodder (AREA)
- Fats And Perfumes (AREA)
Abstract
Description
【発明の詳細な説明】
(a)産業上の利用分野
本発明は、大豆特有の青臭みがなく風味の良い脱脂大豆
およびかかる脱脂大豆を加工して得られる風味の良い組
織状大豆蛋白に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to a defatted soybean that has a good flavor without the grassy odor characteristic of soybeans, and to a textured soybean protein that has a good flavor and is obtained by processing the defatted soybean.
(b)従来の技術
従来から大豆製品の無臭化乃至品質の改良については種
々の方法が試みられている。例えば全粒大豆または荒割
り大豆を常圧100℃以下で温熱処理する方法(特開昭
60−41455.同61187763、同62−29
4057) 、抽出前の大豆を12〜25%に加湿し、
90〜120℃で熱処理する方法(特公昭63−171
19)、生大豆、粗砕大豆を水分8%以下まで乾燥し、
90℃以上に温熱または乾熱する方法(特公昭59−4
8624)などである。(b) Prior Art Various methods have been tried in the past to make soybean products odorless or to improve their quality. For example, a method of heat-treating whole soybeans or roughly split soybeans at normal pressure of 100°C or less (JP-A No. 60-41455, No. 61187763, No. 62-29)
4057), humidify soybeans before extraction to 12-25%,
A method of heat treatment at 90 to 120°C (Special Publication No. 63-171
19), drying raw soybeans and coarsely crushed soybeans to a moisture content of 8% or less,
Method of heating or dry heating to 90℃ or higher
8624).
(C)発明が解決しようとする課題
しかしながら全粒大豆または荒割り大豆を常圧で温熱処
理する方法は、大豆の風味の改善効果が不十分であり、
抽出前の大豆を加湿し熱処理する方法は大豆油の品質改
良を目的としており、脱脂大豆の品質向上には殆ど効果
がない。生大豆、粗砕大豆を乾燥後、温熱または乾熱す
る方法はミールに大豆臭の残存が認められ、満足すべき
ものではない。(C) Problems to be Solved by the Invention However, the method of heat-treating whole soybeans or roughly split soybeans at normal pressure is insufficient in improving the flavor of soybeans;
The method of humidifying and heat-treating soybeans before extraction is aimed at improving the quality of soybean oil, but has little effect on improving the quality of defatted soybeans. The method of heating or drying raw soybeans or coarsely crushed soybeans after drying leaves a soybean odor in the meal, which is not satisfactory.
本発明の目的は、従来の方法に比べ、大豆臭の除去効果
が大きく風味が大幅に改良された脱脂大豆およびこれを
原料とするU繊状大豆蛋白を製造する方法を提供するこ
とにある。An object of the present invention is to provide a method for producing defatted soybeans that have a greater effect of removing soybean odor and a significantly improved flavor than conventional methods, and U-fibrous soybean protein using the defatted soybeans as a raw material.
(d)課題を解決するだめの手段
即ち本発明は、全粒大豆を粗砕し、脱皮後乾熱加熱によ
り水分を6〜9%(重量。以下同様)に乾燥し、圧扁後
、生蒸気を吹き込みながら加熱加圧する機能を備えたス
クリュー押出機を用いて、生蒸気吹き込み量2〜10%
、加熱温度1加熱−150℃の条件下に加熱加圧し、以
下常法により油分を抽出除去することを特徴とする脱脂
大豆の製造法およびかかる脱脂大豆を常法に従って押出
成形機により処理することを特徴とする組織状大豆蛋白
の製造法である。(d) Means to solve the problem, that is, the present invention, consists of coarsely crushing whole soybeans, drying them by dry heat after dehulling to reduce the moisture content to 6 to 9% (by weight; the same applies hereinafter), pressing them, and then Using a screw extruder with the function of heating and pressurizing while blowing steam, the amount of live steam blowing is 2 to 10%.
, a method for producing defatted soybeans characterized by heating and pressurizing at a heating temperature of 1 - 150°C and extracting and removing oil by a conventional method, and processing such defatted soybeans using an extrusion molding machine according to a conventional method. This is a method for producing textured soybean protein characterized by the following.
全粒大豆は粗砕後脱皮されるが、これは脱皮しないと目
的物の風味が悪くなるからである。次に脱脂大…を乾熱
加熱により乾燥する。このためには例えば蒸気による間
接加熱装置などを用いることができる。この工程では乾
熱加熱であることが必要であり、温熱加熱するとその後
の処理によっても大豆臭の除去効果が小さくなってしま
う。全粒大豆の水分は通常11〜13%であるが、これ
を上記の乾熱加熱により6〜9%に乾燥する。9%を超
えると大豆特有の青臭みが残り、6%未満では焦げ臭が
発生し風味を害する。圧扁はロールなどを用いて行い、
厚みは0.5 ms以下が好ましい。Whole soybeans are coarsely crushed and then dehulled, because if the soybeans are not dehulled, the flavor of the desired product will deteriorate. Next, the degreased large piece is dried by dry heat heating. For this purpose, for example, an indirect heating device using steam or the like can be used. This step requires dry heating, and if heated, the effect of removing soybean odor will be reduced even in subsequent treatments. The moisture content of whole soybeans is usually 11 to 13%, but this is dried to 6 to 9% by the above-mentioned dry heat heating. If it exceeds 9%, the grassy odor characteristic of soybeans remains, and if it is less than 6%, a burnt odor will occur and the flavor will be impaired. Compressing is done using a roll etc.
The thickness is preferably 0.5 ms or less.
これより厚いと風味改善効果が落ち、また脱脂大豆の残
油骨が多くなるため、やはり風味の改良が不十分になる
。If it is thicker than this, the flavor improvement effect will be reduced, and the remaining oil bones of the defatted soybeans will increase, resulting in insufficient flavor improvement.
以上のように粗砕、脱皮、乾熱加熱乾燥および圧扁を行
った大豆は、次に一定量の生蒸気を吹き込みながら加熱
加圧する機能を備えたスクリュー押出機を用いて処理す
る。生蒸気の吹き込み量は処理物に対して2〜10%、
加熱温度は100〜150℃であり、生蒸気の量および
加熱温度がこれらの範囲外であると大豆臭の除去効果が
劣る。The soybeans that have been crushed, dehulled, dried by dry heat, and compressed as described above are then processed using a screw extruder equipped with a function of heating and pressurizing the soybean while blowing a certain amount of live steam into the soybean. The amount of live steam blown is 2 to 10% of the processed material.
The heating temperature is 100 to 150°C, and if the amount of live steam and the heating temperature are outside these ranges, the soybean odor removal effect will be poor.
大豆は上記のスクリュー押出機内で機械的な作用を受け
るとともに押出機出口で大気中に放出され、これらが総
合的に作用して大豆臭が除去されるものと推定される。The soybeans are subjected to mechanical action within the above-mentioned screw extruder and are released into the atmosphere at the exit of the extruder, and it is presumed that the soybean odor is removed by the comprehensive action of these factors.
得られた処理大豆は、次いで常法に従ってヘキサンなど
の有機溶媒により油を抽出し、脱脂粕を脱溶剤機で脱溶
剤し、乾燥、冷却して脱脂大豆とする。The obtained treated soybeans are then extracted with an organic solvent such as hexane in accordance with a conventional method, and the defatted lees is desolvented using a desolventizer, dried, and cooled to obtain defatted soybeans.
またこの脱脂大豆を原料として、常法により押出成形機
を用いて加熱加圧し、組織状大豆蛋白を製造する。押出
成形機としては、−軸型、二軸型などが使用でき、温度
80〜200℃、圧力10〜50kg/cm2程度の条
件下に処理する。Using this defatted soybean as a raw material, a textured soybean protein is produced by heating and pressurizing the defatted soybean using an extruder in a conventional manner. As the extrusion molding machine, a -shaft type, a twin-screw type, etc. can be used, and the processing is carried out under conditions of a temperature of 80 to 200°C and a pressure of about 10 to 50 kg/cm2.
(e)実施例および比較例
実施例1
全粒大豆(水分12.5%)を粗砕し、ハルセパレータ
により脱皮し、横型間接加熱機により乾熱条件下に水分
を蒸発させ、水分を8.0%に調整した。ロールで厚さ
0.4mmに圧扁し、直ちに生蒸気を吹き込みながら加
熱加圧する機能を備えたスクリュー押出機を用い、処理
物に対し3%の生蒸気を吹き込みながら温度130℃で
処理し、この後常法に従ってヘキサンにより油を抽出し
、残りの脱脂粕を脱溶剤し、乾燥、冷却して脱脂大豆を
得た。風味をみたところ、大豆特有の青臭い大豆臭は全
く感じられず良い風味であった。(e) Examples and Comparative Examples Example 1 Whole soybeans (moisture 12.5%) were coarsely crushed, dehulled using a hull separator, and water was evaporated under dry heat conditions using a horizontal indirect heating machine to reduce the water content to 8. It was adjusted to .0%. The product was pressed to a thickness of 0.4 mm with rolls, and immediately processed at a temperature of 130°C while blowing 3% live steam into the processed material using a screw extruder equipped with a function of heating and pressurizing while blowing live steam. Thereafter, the oil was extracted with hexane according to a conventional method, and the remaining defatted lees was removed from the solvent, dried, and cooled to obtain defatted soybeans. When I looked at the flavor, I found that it had a good flavor with no green soybean odor characteristic of soybeans.
比較例1
全粒大豆(水分12.5%)を粗砕し脱皮した後、その
ままロールで0.4n+mに圧扁し、直ちに生蒸気を吹
き込みながら加熱加圧する機能を備えたスクリュー押出
機を用い、処理物に対し3%の生蒸気を吹き込みながら
温度130℃で処理し、以後実施例1と同様に処理して
脱脂大豆を得た。風味をみたところ、大豆特有の青臭い
大豆臭が残っており、風味は良くなかった。Comparative Example 1 Whole soybeans (moisture 12.5%) were coarsely crushed and dehulled, then flattened to 0.4n+m with rolls, and immediately heated and pressurized while blowing live steam using a screw extruder. The treated material was treated at a temperature of 130° C. while blowing 3% live steam into it, and thereafter treated in the same manner as in Example 1 to obtain defatted soybeans. When I looked at the flavor, I found that it still had a grassy soybean odor characteristic of soybeans, and the flavor was not good.
比較例2
全粒大豆(水分12.5%)を粗砕し、ハルセパレータ
により脱皮し、横型間接加熱機により乾熱条件下に水分
を蒸発させ、水分を8.0%に調整した。ロールで厚さ
0.4mmに圧扁した後、そのまま常法によりヘキサン
による油の抽出工程を経て、脱溶剤、乾燥、冷却して脱
脂大豆を得た。風味をみたところ、大豆特有の青臭い大
豆臭が残っておリ、風味は良くなかった。Comparative Example 2 Whole soybeans (moisture 12.5%) were coarsely crushed, dehulled using a hull separator, and water was evaporated under dry heat conditions using a horizontal indirect heating machine to adjust the water content to 8.0%. After pressing to a thickness of 0.4 mm with a roll, the soybeans were subjected to an oil extraction process using hexane in a conventional manner, followed by solvent removal, drying, and cooling to obtain defatted soybeans. When I looked at the flavor, I found that it had a grassy soybean odor characteristic of soybeans, and the flavor was not good.
実施例2
実施例1で得た脱脂大豆を原料とし、二輪型エクストル
ーダーにより温度110℃、圧力151g/c112の
条件下に処理して、風味の良い組織状大豆蛋白を得た。Example 2 The defatted soybean obtained in Example 1 was used as a raw material and processed with a two-wheeled extruder at a temperature of 110° C. and a pressure of 151 g/c112 to obtain a textured soybean protein with good flavor.
(f)発明の効果
本発明の脱脂大豆および組織状大豆蛋白の製造法では、
全粒大豆を粗砕した後脱皮し、予め乾熱加熱で水分を6
〜9重量%にしておくことにより、後で行われるスクリ
ュー押出機を用いた加熱加圧処理工程での脱臭効果が飛
躍的に増大し、大豆臭の殆どない脱脂大豆および組織状
大豆蛋白を得ることができる。これに対し、かかる乾熱
加熱を行わず水分を滅じないで処理すると、脱臭効果は
不十分となる。(f) Effects of the invention In the method for producing defatted soybeans and textured soybean protein of the present invention,
After coarsely crushing whole soybeans, they are dehulled, and the moisture is removed by dry heat in advance.
By keeping it at ~9% by weight, the deodorizing effect in the subsequent heating and pressure treatment process using a screw extruder is dramatically increased, and defatted soybeans and textured soybean protein with almost no soy odor can be obtained. be able to. On the other hand, if dry heat heating is not performed and the moisture is not destroyed, the deodorizing effect will be insufficient.
Claims (2)
6〜9重量%に乾燥し、圧扁後、生蒸気を吹き込みなが
ら加熱加圧する機能を備えたスクリュー押出機を用いて
、生蒸気吹き込み量2〜10重量%、加熱温度100〜
150℃の条件下に加熱加圧し、以下常法により油分を
抽出除去することを特徴とする脱脂大豆の製造法。(1) Whole grain soybeans are coarsely crushed, and after dehulling, dry heat is used to dry the water content to 6 to 9% by weight, and after compression, using a screw extruder equipped with the function of heating and pressurizing while blowing live steam. , Live steam injection amount 2-10% by weight, Heating temperature 100-
A method for producing defatted soybeans, which comprises heating and pressurizing under conditions of 150°C and extracting and removing oil by a conventional method.
て押出成形機により処理することを特徴とする組織状脱
脂大豆の製造法。(2) A method for producing a textured defatted soybean, which uses the defatted soybean according to claim 1 as a raw material and processes the defatted soybean according to a conventional method using an extrusion molding machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2232829A JPH04112763A (en) | 1990-09-03 | 1990-09-03 | Preparation of defatted soybean and tissue-like soybean protein |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2232829A JPH04112763A (en) | 1990-09-03 | 1990-09-03 | Preparation of defatted soybean and tissue-like soybean protein |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04112763A true JPH04112763A (en) | 1992-04-14 |
Family
ID=16945441
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2232829A Pending JPH04112763A (en) | 1990-09-03 | 1990-09-03 | Preparation of defatted soybean and tissue-like soybean protein |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04112763A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019189476A1 (en) * | 2018-03-30 | 2019-10-03 | 不二製油グループ本社株式会社 | Production method of textured plant protein material |
| CN117460421A (en) * | 2021-06-22 | 2024-01-26 | 株式会社派利肯 | Full-fat tissue-like protein with excellent storage stability |
-
1990
- 1990-09-03 JP JP2232829A patent/JPH04112763A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019189476A1 (en) * | 2018-03-30 | 2019-10-03 | 不二製油グループ本社株式会社 | Production method of textured plant protein material |
| JPWO2019189476A1 (en) * | 2018-03-30 | 2021-04-08 | 不二製油株式会社 | Method for producing tissue-like vegetable protein material |
| CN117460421A (en) * | 2021-06-22 | 2024-01-26 | 株式会社派利肯 | Full-fat tissue-like protein with excellent storage stability |
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