JPS6135819B2 - - Google Patents

Info

Publication number
JPS6135819B2
JPS6135819B2 JP54092745A JP9274579A JPS6135819B2 JP S6135819 B2 JPS6135819 B2 JP S6135819B2 JP 54092745 A JP54092745 A JP 54092745A JP 9274579 A JP9274579 A JP 9274579A JP S6135819 B2 JPS6135819 B2 JP S6135819B2
Authority
JP
Japan
Prior art keywords
mustard
lees
seeds
oil
extraction
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
Application number
JP54092745A
Other languages
Japanese (ja)
Other versions
JPS5618565A (en
Inventor
Shingo Fujiwara
Yukitane Ko
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.)
TSUJI SEIYU KK
Original Assignee
TSUJI SEIYU KK
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 TSUJI SEIYU KK filed Critical TSUJI SEIYU KK
Priority to JP9274579A priority Critical patent/JPS5618565A/en
Publication of JPS5618565A publication Critical patent/JPS5618565A/en
Publication of JPS6135819B2 publication Critical patent/JPS6135819B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はからしの製造法に係り、特にからし中
の辛味成分をそれの製造工程中において有効に保
存し、且つ使用時にはそれ特有の鋭い辛味を高め
得ると共に、原料種子中に含まれる油脂分の有効
利用を図り得る方法を提供するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing mustard, and in particular, it is possible to effectively preserve the pungent components in mustard during the production process, and to enhance the characteristic sharp pungent taste during use. The present invention provides a method for effectively utilizing oil and fat contained in raw material seeds.

香辛料などに供せられるからしはアブラナ科植
物に属するカラシナ類、例えば黒からし、白から
し、日本からしなどの種子から得られる。具体的
には、これらからしの熟した実を圧搾してそれに
多量に含まれる油脂を除き、ついで得られた圧搾
粕を乾燥、粉砕し、微粉にして作られる。このよ
うな従来からの製造法において、搾油方法として
圧搾法を採用している理由は、からしが高温で処
理されるとからしの有効成分が揮発散逸するため
である。しかも、この圧搾法でも摩擦熱による熱
発生の少ない機構、例えばケージプレスなどを採
用して圧搾することが望ましく、そして良質のか
らしを得るためには60℃以下の温度で処理するこ
とがよいとされている。
Mustard, which is used as a spice, is obtained from the seeds of mustard plants belonging to the Brassica family, such as black mustard, white mustard, and Japanese mustard. Specifically, these ripe mustard fruits are pressed to remove the large amount of oil and fat contained therein, and the resulting pressed lees is then dried and crushed to form a fine powder. In such conventional production methods, the reason why the expression method is employed as the oil extraction method is that when mustard is treated at high temperatures, the active ingredients of mustard are volatilized and dissipated. Moreover, even with this pressing method, it is desirable to use a mechanism that generates less heat due to frictional heat, such as a cage press, and to obtain high-quality mustard, it is preferable to process at a temperature of 60°C or lower. It is said that

しかしながら、この従来の圧搾法によるからし
の製造法は能率が悪く、また圧搾後の搾油粕たる
からし中には未だ15〜18%の油分(油脂)が残つ
ており、原料種子中に含まれる油分30乃至35%の
約半分が除かれているに過ぎないのである。従つ
て、この従来の圧搾法は、種子中の油分の有効利
用の面からして不十分であるばかりでなく、から
し特有の鋭い辛味をもたせるためには油脂分を少
なくすることがよいとされている点からしても、
最上の方法とは言えず、なおその改善が望まれて
いるのである。
However, this conventional method of producing mustard using the pressing method is inefficient, and 15 to 18% of oil (fat) still remains in the mustard oil lees after pressing, which is not included in the raw material seeds. Only about half of the 30 to 35% oil contained in the oil is removed. Therefore, this conventional pressing method is not only insufficient in terms of effective utilization of the oil content in the seeds, but also that it is better to reduce the oil content in order to obtain the sharp pungent taste unique to mustard. From the point of view of
Although it is not the best method, improvements are still desired.

一方、植物油脂の搾油法として知られる他の一
般的な方法に抽出法があり、搾油効率の点におい
て先の圧搾法より揺かに優れていることが認めら
れているが、搾油粕としての抽出粕に残存する溶
剤、例えばn―ヘキサンなどを完全に除去するた
めには、工業的規模においては高温の加熱工程の
採用は避けられず、それ故かかる抽出法はからし
の製造においては適さないものとされているので
ある。
On the other hand, the extraction method is another common method known for extracting vegetable oils and fats, and it is recognized that it is far superior to the previous pressing method in terms of oil extraction efficiency. In order to completely remove the solvent remaining in the extraction lees, such as n-hexane, it is unavoidable to employ a high-temperature heating process on an industrial scale, and therefore such an extraction method is not suitable for mustard production. It is considered that there is no such thing.

周知のように、からしの辛味は、からし中に含
まれる配糖体シニグリン(黒からしの場合)が同
じくからし成分中の酵素ミロシナーゼ(ミロシ
ン)の加水分解作用によつて生成するイソチオシ
アン酸アリルの働きにより、発揮されている。
As is well known, the spiciness of mustard is due to the isothiocyanide produced by the hydrolysis of the glycoside sinigrin (in the case of black mustard) of the enzyme myrosinase (myrosin), which is also a component of mustard. It is exerted by the action of allyl acid.

従つて、からし(粉末)を香辛料として用いる
場合には、それの使用に際しての水練りを行なう
ときに初めて上記の反応が惹起され、それ以前に
おいては配糖体の形でイソチオシアン酸アリルが
保存されていなければならず、また分解酵素とし
てのミロシナーゼも同様に保存されていなければ
ならない。
Therefore, when mustard (powder) is used as a spice, the above reaction occurs only when it is kneaded with water before use, and before that, allyl isothiocyanate is stored in the form of glycosides. In addition, myrosinase as a degrading enzyme must be conserved as well.

ここにおいて、本発明者らは、かかる事情に鑑
み、からし中の辛味成分を有効に保存し得るから
しの製造法について鋭意検討した結果、上記反応
の進行を極力抑えて配糖体の状態が搾油後も良好
に保存されるような、酵素作用が効果的に抑制さ
れ得る手法を見い出し、本発明に到達したのであ
る。
In view of the above circumstances, the present inventors have conducted intensive studies on a method for producing mustard that can effectively preserve the pungent components in mustard, and have found that the progress of the above reaction can be suppressed as much as possible to maintain the state of glycosides. The present invention was achieved by discovering a method for effectively suppressing the enzyme action so that the oil is well preserved even after oil extraction.

すなわち、本発明は、カラシナ類の種子からそ
れに含まれる油脂を抽出法により搾油した後、そ
の抽出粕に減圧水蒸気蒸留を施してかかる抽出粕
に残留する前記抽出法で用いられた溶剤を除去せ
しめ、ついで低温乾燥を施すことにより、からし
を製造するようにしたものであり、これによつて
からし原料種子よりの油脂分の搾油を効率的に行
ない、ひいてはかかる油脂の有効利用を図る一
方、辛味成分たるシニグリンなどの配糖体を製造
工程中において有効に保存し、しかも分解酵素と
してのミロシナーゼも活性な形で保存し得ること
となり、以てその使用時に前記反応を効果的に進
行せしめ得て最大限にその辛味を発揮させ得るこ
ととなつたのである。
That is, the present invention involves extracting the oils and fats contained therein from mustard seeds by an extraction method, and then subjecting the extracted lees to vacuum steam distillation to remove the solvent used in the extraction method remaining in the extraction lees. Then, mustard is produced by drying at a low temperature, thereby efficiently extracting the oil and fat from the mustard raw material seeds, and thereby making effective use of the oil and fat. , it is possible to effectively preserve glycosides such as sinigrin, which is a pungent component, during the manufacturing process, and also preserve myrosinase, which is a degrading enzyme, in an active form, thereby allowing the above reaction to proceed effectively when used. As a result, it was possible to bring out its spiciness to the fullest.

かかる本発明方法に従えば、先ず黒からし、白
からし、日本からし等のカラシナ類の熟した乾燥
種子には、適当な抽出溶剤を用いた抽出燥作が施
されることとなる。具体的には、公知の抽出手法
の如く、原料種子は一般に圧扁ロール機により非
常に薄いフレーク状に圧扁された後、抽出機に送
り込まれ、そこでn―ヘキサンなどの適当な溶剤
に浸漬または浸透させられることによつて、かか
る種子中に含まれる油脂分が抽出されるのであ
る。なお、この原料種子に対する圧扁は該種子か
らの油脂分の抽出を効果的に行なうためのもので
あつて、その他これに代えて適当な破砕若しくは
粉砕手段を採用することが可能である。また、圧
扁された種子を抽出機にかけて抽出操作を施すに
先立つて予備圧搾を行ない、ついで抽出機にかけ
るような手法を採用しても何等差支えない。
According to the method of the present invention, ripe dried seeds of mustards such as black mustard, white mustard, and Japanese mustard are first subjected to extraction drying using an appropriate extraction solvent. Specifically, as in the known extraction method, raw seeds are generally pressed into very thin flakes using a pressing roll machine, and then fed into an extractor, where they are soaked in a suitable solvent such as n-hexane. Alternatively, the oils and fats contained in the seeds are extracted by being permeated. Note that this pressing of the raw material seeds is for effectively extracting oil and fat from the seeds, and other appropriate crushing or pulverizing means may be employed instead. Furthermore, there is no problem in adopting a method in which the pressed seeds are subjected to preliminary compression before being subjected to the extraction operation by applying them to an extractor, and then being applied to the extractor.

そして、抽出機における所定の抽出操作が施さ
れた後、該抽出機から取り出された抽出粕は、通
常30%ほどの溶剤を含んでいるので、脱溶剤機に
て機械的に先ず脱溶剤され、該抽出粕中の溶剤の
一部が回収されることとなるが、この操作で除去
し得なかつた該抽出粕中に未だ残留する溶剤は、
更に次の本発明に従う減圧水蒸気蒸留工程にて効
果的に回収されるのである。
After the predetermined extraction operation in the extractor has been performed, the extracted lees taken out from the extractor usually contains about 30% solvent, so it is first mechanically desolventized in a desolventizer. , a part of the solvent in the extracted lees will be recovered, but the solvent that still remains in the extracted lees that could not be removed by this operation is
Furthermore, it is effectively recovered in the next step of reduced pressure steam distillation according to the present invention.

すなわち、かかる溶剤がある程度残留する抽出
粕に対して、水蒸気蒸留を減圧下において施すこ
とにより、低温度下で溶剤を完全に留去せしめよ
うとするものであつて、これにより活性な形で分
解酵素ミロシナーゼを保存しつつ、高温下での水
分との接触を避けるようにして該抽出粕中の辛味
成分(配糖体)の分解を効果的に阻止し、以て該
辛味成分の有効な保存を図り得たのである。な
お、この減圧水蒸気蒸留は、一般に100℃以下、
特に60℃以下、更に好ましくは40℃以下において
行なうことが望ましく、これによつてより有効な
酵素の性状態の保持並びに辛味成分の保存が可能
となるのである。また、減圧度としては、一般に
50mmHg以下、好ましくは30mmHg以下の値が好
適に採用されることとなる。
In other words, by subjecting the extracted lees in which a certain amount of the solvent remains to steam distillation under reduced pressure, the solvent is completely distilled off at low temperature, thereby decomposing it in an active form. While preserving the enzyme myrosinase, the decomposition of the pungent components (glycosides) in the extracted lees is effectively prevented by avoiding contact with moisture at high temperatures, thereby effectively preserving the pungent components. We were able to achieve this. Note that this reduced pressure steam distillation is generally carried out at temperatures below 100°C.
In particular, it is desirable to carry out the heating at a temperature of 60°C or lower, more preferably 40°C or lower, as this makes it possible to more effectively maintain the state of the enzyme and preserve the pungent component. In addition, the degree of decompression is generally
A value of 50 mmHg or less, preferably 30 mmHg or less will be suitably employed.

ついで、かかる減圧水蒸気蒸留によつて脱溶剤
された抽出粕には乾燥操作が施されて、該粕に含
まれる水分が除かれるが、この乾燥は低温におい
て行なう必要があるのであり、その乾燥温度を高
くすると、せつかくそれまで保存されてきた酵素
活性を減少せしめ、ひいては辛味の充分な発揮を
困難にする。特に、この低温乾燥には、60℃以下
の乾燥空気を用いたり、或は60℃以下の減圧乾燥
手法などが好適に採用されることとなる。
Next, the extracted lees from which the solvent has been removed by such vacuum steam distillation is subjected to a drying operation to remove the moisture contained in the lees, but this drying must be carried out at a low temperature. If the temperature is increased, the enzymatic activity that has been preserved until then will be reduced, making it difficult to fully develop the spiciness. In particular, for this low-temperature drying, use of dry air at 60° C. or lower, or reduced pressure drying at 60° C. or lower is preferably employed.

そして、かくして得られた乾燥粕は、必要に応
じて表皮が取り除かれ、粉砕されて、粉末状のか
らしに製品化されることとなるが、かかるからし
製品には、その製造工程中における高温での水と
の接触が極力回避されているために、辛味成分た
る配糖体が散逸することなく有効に保存されてい
ると同時に、分解酵素たるミロシナーゼも活性な
状態で保存されており、それ故その使用時におけ
る水練りによつて初めて先の加水分解反応が効率
的に進行し、良好なからしの風味が発現されるの
である。また、かかるからし製品は、従来のもの
とは異なり油脂分の含量が著しく低く、しかもそ
の含量が自由に制御され得るために、からし特有
の鋭い辛味を効果的に与え得ると同時に、その程
度も任意に制御され得るのである。さらに、この
ような油脂分の含量の低下により、からしが長期
間に亘つて貯蔵されてもその香辛味を極端に失な
うようなこともないのである。
The dried lees obtained in this way will be manufactured into powdered mustard by removing the epidermis and pulverizing as necessary. Because contact with water at high temperatures is avoided as much as possible, the glycosides, which are the pungent component, are effectively preserved without escaping, and at the same time, the degrading enzyme myrosinase is also preserved in an active state. Therefore, by kneading with water during use, the hydrolysis reaction proceeds efficiently and a good mustard flavor is developed. In addition, unlike conventional products, such mustard products have a significantly low oil and fat content, and since the content can be freely controlled, they can effectively impart the sharp spiciness characteristic of mustard, while at the same time The degree can also be controlled arbitrarily. Furthermore, due to such a reduction in the fat and oil content, mustard does not lose its spiciness significantly even if it is stored for a long period of time.

また一方、前記抽出工程において圧扁種子から
溶剤抽出された油脂分は、蒸留などの操作によつ
て、それから溶剤(n―ヘキサンなど)が除去せ
しめられ、そしてデガミング工程(ガム質のもの
を取り出す工程)などを経て、芥子油として取り
出されることとなるが、抽出法本来の特徴に基づ
き圧扁種子からはそこに含まれる油脂分の大部分
が効率的に採取されるので、該種子中の油脂分の
有効な利用も図り得ることとなつたのである。
On the other hand, the solvent (n-hexane, etc.) is removed from the oils and fats extracted from the pressed seeds in the extraction process by distillation, etc., and then the degumming process (removal of gummy seeds) is carried out. However, based on the original characteristics of the extraction method, most of the oils and fats contained in the crushed seeds are efficiently extracted, so the oil in the seeds is It has also become possible to effectively utilize fats and oils.

次に、本発明を更に具体的に明らかにするため
に実施例を示すが、本発明がかかる実施例によつ
て何等の制限をも受けるものでないことは言うま
でもない。なお、実施例中、部及び百分率は特に
断わりのない限りすべて重量基準である。
Next, Examples will be shown to clarify the present invention more specifically, but it goes without saying that the present invention is not limited in any way by these Examples. In the examples, all parts and percentages are based on weight unless otherwise specified.

実施例 乾燥した黒からしの実を圧扁ロールにかけてフ
レーク状と為した。ついで、このフレーク状の実
400部を所定の抽出装置に入れ、n―ヘキサン
1200部に常温下、15分間浸漬して抽出操作を施し
た後、抽出液を払い出した。そして、この操作を
再度繰り返した。
Example Dried black mustard seeds were rolled into flakes. Next, this flaky fruit
Put 400 parts into the specified extraction device and add n-hexane.
After performing an extraction operation by immersing the sample in 1200 parts at room temperature for 15 minutes, the extract was discharged. This operation was then repeated again.

ついで、かかる抽出粕を減圧水蒸気蒸留装置に
入れ、毛管を通じて該装置に水蒸気を吹き込む一
方、真空ポンプで吸引して約20mmHgの減圧度に
て減圧水蒸気蒸留を施すことにより、該抽出粕中
の残留溶剤(n―ヘキサン)を完全に除去した。
そして、この脱溶剤された抽出粕に対して、約50
℃の温度の乾燥空気を吹込むことにより、該粕中
の水分率が7%になるまで乾燥操作を施した。
Next, the extracted lees is placed in a vacuum steam distillation device, and while steam is blown into the device through a capillary tube, the residue in the extracted lees is removed by suctioning with a vacuum pump and performing vacuum steam distillation at a reduced pressure of about 20 mmHg. The solvent (n-hexane) was completely removed.
Approximately 50%
A drying operation was carried out by blowing dry air at a temperature of .degree. C. until the moisture content in the lees reached 7%.

かくして得られた乾燥粕を粉砕機で粉砕した
後、生成した粉末の一部を少量の水で練つたとこ
ろ、市販のからしと同等またはそれ以上の辛味を
呈するものであることが認められた。
After pulverizing the dried lees obtained in this way using a pulverizer, a portion of the resulting powder was kneaded with a small amount of water, and it was found that it had a spiciness equal to or greater than that of commercially available mustard. .

また、からし中のイソチオシアン酸アリルの含
有量を定量するために、上記得られたからし粉末
1部に対して5部の割合で水を加えて40℃、2時
間保持した後、遊離したイソチオシアン酸アリル
を水と共に蒸留分離し、第三版食品添加物公定書
に基づく試験方法に準じて測定したところ、含有
イソチオシアン酸アリルは1.4%と、著しく高い
値を示した。
In addition, in order to quantify the content of allyl isothiocyanate in mustard, water was added at a ratio of 5 parts to 1 part of the mustard powder obtained above and held at 40°C for 2 hours. When allyl acid was separated by distillation along with water and measured according to the test method based on the Third Edition of the Japanese Food Additives Official Standards, the content of allyl isothiocyanate was 1.4%, a significantly high value.

Claims (1)

【特許請求の範囲】 1 カラシナ類の種子からそれに含まれる油脂を
抽出法により搾油した後、その抽出粕に減圧水蒸
気蒸留を施してかかる抽出粕に残留する前記抽出
法で用いられた溶剤を除去せしめ、ついで低温乾
燥を施すことを特徴とするからしの製造法。 2 前記減圧水蒸気蒸留が、約100℃以下の温度
下において行なわれる特許請求の範囲第1項記載
の製造法。 3 前記低温乾燥が、約60℃以下の温度下におい
て行なわれる特許請求の範囲第1項記載の製造
法。
[Scope of Claims] 1. After extracting the oils and fats contained therein from mustard seeds by an extraction method, the extracted lees is subjected to vacuum steam distillation to remove the solvent used in the extraction method remaining in the extracted lees. A mustard production method characterized by drying and then low-temperature drying. 2. The production method according to claim 1, wherein the reduced pressure steam distillation is performed at a temperature of about 100°C or less. 3. The manufacturing method according to claim 1, wherein the low-temperature drying is performed at a temperature of about 60° C. or lower.
JP9274579A 1979-07-20 1979-07-20 Preparation of mustard Granted JPS5618565A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9274579A JPS5618565A (en) 1979-07-20 1979-07-20 Preparation of mustard

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9274579A JPS5618565A (en) 1979-07-20 1979-07-20 Preparation of mustard

Publications (2)

Publication Number Publication Date
JPS5618565A JPS5618565A (en) 1981-02-21
JPS6135819B2 true JPS6135819B2 (en) 1986-08-15

Family

ID=14062944

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9274579A Granted JPS5618565A (en) 1979-07-20 1979-07-20 Preparation of mustard

Country Status (1)

Country Link
JP (1) JPS5618565A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63142106U (en) * 1987-03-10 1988-09-19

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FR2717492B1 (en) * 1994-03-15 1996-04-12 Commissariat Energie Atomique Method and installation for extracting an essential oil from plants.
IL130303A0 (en) 1999-06-03 2000-06-01 M G Novobiotech Ltd A bacterial strain processed plant extracts and probiotic compositions for human and veterinary use
JP4782620B2 (en) * 2005-06-22 2011-09-28 築野食品工業株式会社 Method for producing low-denatured defatted rice bran

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63142106U (en) * 1987-03-10 1988-09-19

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JPS5618565A (en) 1981-02-21

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