JPS5948064A - Preparation of extract of sesame - Google Patents

Preparation of extract of sesame

Info

Publication number
JPS5948064A
JPS5948064A JP57160640A JP16064082A JPS5948064A JP S5948064 A JPS5948064 A JP S5948064A JP 57160640 A JP57160640 A JP 57160640A JP 16064082 A JP16064082 A JP 16064082A JP S5948064 A JPS5948064 A JP S5948064A
Authority
JP
Japan
Prior art keywords
extract
water
ethanol
sesame
weight
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
JP57160640A
Other languages
Japanese (ja)
Other versions
JPS6126342B2 (en
Inventor
Tatsuhiko Ozaki
尾崎 龍彦
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.)
Takemoto Oil and Fat Co Ltd
Original Assignee
Takemoto Oil and Fat 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 Takemoto Oil and Fat Co Ltd filed Critical Takemoto Oil and Fat Co Ltd
Priority to JP57160640A priority Critical patent/JPS5948064A/en
Publication of JPS5948064A publication Critical patent/JPS5948064A/en
Publication of JPS6126342B2 publication Critical patent/JPS6126342B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain an extract having extremely effective effect on prevention of change of properties by a very simple method, by extracting ground seed of sesame by a proper combination of extraction operations selecting ethanol-containing aqueous solvents. CONSTITUTION:100pts.wt. ground sesame seed such as defatted sesame seed, pressed sesame seed, etc. is extracted with >=250pts.wt. water alone or mixed solvent of ethanol and water containing >=5wt% water at room temperature - 50 deg.C. Unstable materials are removed from this extract by operations such as filtration, centrifugation, etc. to give an extracted solution, which is concentrated or dried. The concentration or drying is carried out until the total amount becomes <=40pts.wt. and the water content in the remaining solvent is >=50wt%. The condensate or dried material is extracted again with ethanol alone or a mixed solvent of ethanol and water. In this case, a weight ratio of ethanol and water is (100:0)-(60:40), and the total amount is <=100pts.wt. Consequently, an extract of sesame capable of preventing oxidation of foods, change of properties, etc. extremely effectively can be obtained.

Description

【発明の詳細な説明】 本発明は胡麻抽出物の製造方法、更に詳しくは食品の酸
化劣化や退色等による変質を極めて有効に防止し得る胡
麻抽出物の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a sesame extract, and more particularly to a method for producing a sesame extract that can extremely effectively prevent deterioration of foods due to oxidative deterioration and discoloration.

食用油脂及びこれを含有する加工食品がその加工段階及
び保存中に油脂の自動酸化により鮮度の低下や変敗等を
起すことはよく知られている。しだがって、これらの油
脂や油脂含有加工食品、例えば大豆油、胡麻油、ナタネ
油、サフラワー油、ヤシ油、チキンオイル、ラード又は
魚油等の動植物油脂や、ドレッシング、マヨネーズ、シ
ョートニング、チーズ、バター、マーカリン、ハム、ソ
ーセージ、即席中華麺又は揚菓子等の含油加工食品、に
おいては酸化防止に対する何等かの対策を施すのが常で
ある。また、ジュースや炭酸飲料等、天然あるいは加工
飲料等においても天然に又は添加剤として含まれるカロ
チン類をはじめとする色素や着色料の日光や人工光源等
で助長される退色現象がみられ、これらについても同様
にその退色防止のだめの何らかの対策が必要である。
It is well known that edible fats and oils and processed foods containing them lose their freshness and deteriorate due to autooxidation of the fats and oils during processing and storage. Therefore, these fats and oil-containing processed foods, such as animal and vegetable oils and fats such as soybean oil, sesame oil, rapeseed oil, safflower oil, coconut oil, chicken oil, lard or fish oil, dressings, mayonnaise, shortening, cheese, In oil-containing processed foods such as butter, marcarin, ham, sausage, instant Chinese noodles, and fried sweets, some kind of measure to prevent oxidation is usually taken. In addition, discoloration of pigments and colorants such as carotenes naturally contained or as additives is observed in natural or processed beverages such as juices and carbonated drinks, which is facilitated by sunlight and artificial light sources. Similarly, it is necessary to take some measures to prevent color fading.

従来、このような食品類の酸化劣化や退色等による変質
に対して、食品の品質維持を図るために各種の酸化防止
剤の類が食品添加物として広く使用されている。
Conventionally, various antioxidants have been widely used as food additives in order to maintain the quality of foods against such deterioration due to oxidative deterioration, discoloration, etc. of foods.

ところが、この種の食品添加物は天然及び人工と多岐に
わたるが、安全性に優れている天然品はその変質防止性
能において充分でなく、人工島については特に最近その
安全性につき見直しが強調されていて、実情はより安全
性が高く且つ酸化劣化や退色等による変質に対してその
防止性能に優れたものの出現が強く望まれているのであ
る。
However, there are a wide variety of food additives of this kind, both natural and artificial, but natural products, which are highly safe, do not have sufficient performance in preventing deterioration, and recently there has been an emphasis on reconsidering the safety of artificial islands. Therefore, in reality, there is a strong desire for a material that is safer and has an excellent ability to prevent deterioration due to oxidative deterioration and discoloration.

本発明者等は、かかる実情に鑑みて、安全性の高い優れ
た変質防止成分を得るため、胡麻種子中に含まれる各種
の成分に着目して、これらを有効に採取する方法に関し
鋭意研究した結果、脱脂胡麻種子あるいは圧ぺんされた
胡麻種子等の破砕された胡麻種子より、特定の溶媒を選
定して抽出操作を適宜に組合せることにより、非常に簡
便な方法で極めて有効な変質防止効果を有する抽出物が
得られることを見出し、本発明を完成するに至った。
In view of these circumstances, the present inventors focused on the various components contained in sesame seeds and conducted intensive research on methods for effectively collecting them, in order to obtain highly safe and excellent deterioration-preventing components. As a result, by selecting a specific solvent and appropriately combining extraction operations from crushed sesame seeds such as defatted sesame seeds or pressed sesame seeds, a very simple method has an extremely effective deterioration prevention effect. It was discovered that an extract having the following properties can be obtained, and the present invention was completed.

すなわち本発明は、食品類の変質防止剤として有効な胡
麻抽出物の製造方法を提供するもので、脱脂胡麻種子又
は圧ぺんされた胡麻種子等の破砕されだ胡麻種子100
重量部に対し、水単独或いは5重量係以上の水を含有す
るエタノール−水混合溶媒を250重量部以上加えて抽
出し、不溶分を除去した後、得られる抽出液を濃縮或い
は乾燥して該抽出液が40重量部以下且つ残留溶媒中の
含水量が50重量%以上になるようにし、次いでエタノ
ール単独或いはエタノール−水混合溶媒を加え、エタノ
ール:水の重量比が100:O〜6040の範囲の溶媒
とし且つ全量が100重量部以下になる範囲で再度抽出
することを特徴とする、食品の酸化劣化や退色等による
変質を極めて有効に防止し得る胡麻抽出物の製造方法に
係る。
That is, the present invention provides a method for producing a sesame extract that is effective as an agent for preventing deterioration of foods.
Extract by adding at least 250 parts by weight of water alone or a mixed solvent of ethanol and water containing 5 parts by weight or more of water to the parts by weight, remove insoluble matter, and concentrate or dry the resulting extract. Adjust the extract so that the amount is 40 parts by weight or less and the water content in the residual solvent is 50% by weight or more, then add ethanol alone or a mixed solvent of ethanol and water so that the weight ratio of ethanol:water is in the range of 100:0 to 6040. The present invention relates to a method for producing a sesame extract that can extremely effectively prevent deterioration of foods due to oxidative deterioration, discoloration, etc., which is characterized in that the sesame extract is extracted again in a range where the total amount is 100 parts by weight or less.

本発明における胡麻抽出物は、前記した如く胡麻の種子
を水若しくはエタノール単独、又ハエタノールー水から
なる混合溶媒を用いて二回に亘り抽出されるもので、使
用する溶媒の特性により油溶性物質を殆んど含有してい
ない。すなわち該抽出物は、油脂類に含有される天然の
抗酸化性物質として従来知られている例えばトコフェロ
ール類やセザモール等を実質的に効果の発現できる程度
には含有しておらず、食品類に対して実質的な変質防止
効果を有する成分が、前記したような天然抗酸化性物質
と異なり、水又はエタノール可溶性成分であるところに
特長を有するものである。
The sesame extract in the present invention is obtained by extracting sesame seeds twice using water or ethanol alone, or a mixed solvent consisting of ethanol and water, as described above, and the oil-soluble substances may be extracted depending on the characteristics of the solvent used. Contains almost no In other words, the extract does not contain tocopherols, sezamol, etc., which are conventionally known as natural antioxidant substances contained in oils and fats, to the extent that they can exhibit substantial effects, and are not suitable for foods. However, unlike the above-mentioned natural antioxidant substances, the component that has a substantial effect of preventing deterioration is a water- or ethanol-soluble component.

以下、本発明の構成を更に詳細に説明する。Hereinafter, the configuration of the present invention will be explained in more detail.

本発明において用いる原料は、得られる胡麻抽出物にと
って不要である油脂類の含有率が低い点で脱脂胡麻種子
が好ましい。胡麻種子を胡麻油と脱脂胡麻種子とに分別
する搾油には種々の方法があり、通常は胡麻種子をその
まま或いは一旦焙煎した後に高圧で機械的に搾油するが
、場合によっては搾油後の脱脂胡麻種子を更にヘキサン
で抽出することもある。本発明で用いる原料は、焙煎の
有無や溶媒抽出の有無等に関係なく、いずれの脱脂胡麻
種子でもよい。また、脱脂前の胡麻種子も適用できるが
、この場合は抽出効果の点で圧べんされたものを用いる
As the raw material used in the present invention, defatted sesame seeds are preferable because they have a low content of oils and fats that are unnecessary for the resulting sesame extract. There are various methods of oil extraction that separate sesame seeds into sesame oil and defatted sesame seeds. Usually, the oil is extracted mechanically under high pressure from sesame seeds as they are or after roasting them, but in some cases defatted sesame seeds are extracted after oil extraction. Seeds may also be extracted with hexane. The raw material used in the present invention may be any defatted sesame seeds, regardless of whether or not they have been roasted or extracted with a solvent. In addition, sesame seeds before defatting can also be used, but in this case, pressed seeds are used for better extraction effectiveness.

本発明はこれらの原料を用いて前後二回の抽出を行うも
のである。−回目の抽出は、原料100重量部に対し、
水単独或いは5重量係以上の水を含有するエタノール−
水混合溶媒を250重量部以上加えて行う。抽出溶媒の
含水量が高くなるほと、原料が膨潤して抽出液の収率が
低下するため、使用する溶媒量を増す方がよく、50重
量係以上の水を含有する溶媒を使用する場合には400
重量部以上の溶媒で抽出するのが好ましい。但し、10
00重量部以上の溶媒を使用しても抽出効果はそれほど
上がらず、後の濃縮又は乾燥の点でも不利となり実際的
でなt/−1゜逆に、エタノール含量の多い溶媒を使用
する場合は該溶媒量が前述の条件範囲内で少なくてもよ
いが、エタノール含量が95重量係を越える溶媒を使用
すると、原料中の残留油分が主として抽出されるように
なり、抗酸化等変質防止性能顛おいて比活性の高い抽出
物をノ 得ることができず、油分以外の有効成分の収率も極端に
低くなる。−回目の抽出に、おいて、溶媒組成及び原料
に対するその使用量以外は特に限定されす、例えば抽出
の最適時間は装置その他の条件によシ大きく変動するの
で適宜選定するが、抽出温度は天然物の変質を防ぐため
に室温〜5o℃の範囲で行うのがよい。前述の範囲内で
抽出条件を変えると、−回目の抽出物の内容はその抽出
条件によって多少異なってくるが、該抽出物に後述する
二回目の抽出操作を加えることによって最終抽出物の内
容の変動を抑えることができるので問題はない。
In the present invention, these raw materials are used for two extractions, one before and one after. - In the second extraction, for 100 parts by weight of the raw material,
Ethanol containing water alone or 5 parts by weight or more of water.
This is carried out by adding 250 parts by weight or more of a water mixed solvent. As the water content of the extraction solvent increases, the raw materials swell and the yield of the extract decreases, so it is better to increase the amount of solvent used, and when using a solvent containing water of 50% by weight or more. 400 for
It is preferable to extract with a solvent in an amount of 1 part by weight or more. However, 10
Even if a solvent of 00 parts by weight or more is used, the extraction effect will not be improved so much, and it will be disadvantageous in terms of subsequent concentration or drying, making it impractical.On the other hand, when using a solvent with a high ethanol content, The amount of the solvent may be small within the above-mentioned condition range, but if a solvent with an ethanol content exceeding 95% by weight is used, the residual oil in the raw material will be mainly extracted, and the antioxidant performance and other deterioration prevention performance will be reduced. Therefore, it is impossible to obtain an extract with high specific activity, and the yield of active ingredients other than oil becomes extremely low. - For the second extraction, there are no particular limitations on anything other than the solvent composition and the amount used for the raw materials. For example, the optimal extraction time varies greatly depending on the equipment and other conditions, so it is selected as appropriate, but the extraction temperature is In order to prevent deterioration of the product, it is preferable to carry out the process at a temperature ranging from room temperature to 5oC. If the extraction conditions are changed within the above-mentioned range, the contents of the -th extract will differ somewhat depending on the extraction conditions, but by adding the second extraction operation described below to the extract, the contents of the final extract will change. There is no problem because the fluctuation can be suppressed.

一回目の抽出で得られるスラリーを濾過や遠心分離等の
操作で抽出液と不溶分とに分離し、次いで抽出液を濃縮
又は乾燥する。濃縮又は乾燥方法についても特に限定さ
れるものではないが、抽出液は糖類や少量の蛋白質を含
むので、これらの変質や着色を防ぐためできるだけ低温
で行うことが好ましい。この際の濃縮は、次の二回目の
抽出に支障のない範囲で溶媒の一部を残留したi!まで
終了してもよいが、最終の抽出効果の点で全量が40重
量部以下且つ残留溶媒中の含水量が50重量%以上にな
るまで行うことが必要である。濃縮物中の残留溶媒が水
含量100重量%に近似する程度のものとなる場合には
全量が30重量部以下まで濃縮しておくことが最終の抽
出効果の点で好ましい。
The slurry obtained from the first extraction is separated into an extract and an insoluble component by filtration, centrifugation, etc., and then the extract is concentrated or dried. There are no particular limitations on the concentration or drying method, but since the extract contains sugars and small amounts of proteins, it is preferable to carry out the concentration or drying at as low a temperature as possible to prevent deterioration and coloration of these substances. At this time, the concentration was such that some of the solvent remained within the range that did not interfere with the next second extraction. However, in view of the final extraction effect, it is necessary to continue until the total amount is 40 parts by weight or less and the water content in the residual solvent is 50% by weight or more. When the residual solvent in the concentrate has a water content of approximately 100% by weight, it is preferable to concentrate the total amount to 30 parts by weight or less in terms of the final extraction effect.

かくして得られる濃縮物又は乾燥物を対象に二回目の抽
出を行う。すなわち、濃縮物又は乾燥物にエタノール単
独或いはエタノール−水の混合溶媒を加え、抽出の際の
溶媒組成がエタノール 水の重量比で100:O〜60
40の範囲になり且つ全量が100重量部以下となる範
囲で抽出する。溶媒組成中のエタノールの含有比率が6
0係より少ない範囲又は全量が100重量部より多い範
囲では抗酸化性等変質防止性能において不活性な成分を
有効に除去できない。但し、有効成分の抽出効果の点で
、全量を15重量部以上として抽出することが実際的で
ある。二回目の抽出において、使用する溶媒組成や量関
係を除き、その抽出条件は前述の一回目の抽出条件と同
様である。
A second extraction is performed on the concentrate or dried product thus obtained. That is, ethanol alone or a mixed solvent of ethanol and water is added to the concentrate or dried material, and the solvent composition during extraction is adjusted to a weight ratio of ethanol to water of 100:O to 60.
40 and the total amount is 100 parts by weight or less. The content ratio of ethanol in the solvent composition is 6
If the ratio is less than 0, or if the total amount is more than 100 parts by weight, inactive components such as antioxidant properties cannot be effectively removed. However, in terms of the effectiveness of extracting the active ingredients, it is practical to extract the total amount at 15 parts by weight or more. In the second extraction, the extraction conditions are the same as those for the first extraction, except for the solvent composition and amount used.

二回目の抽出後、−回目の抽出と同様に不溶分を分離し
、得られる抽出液はそのま1濃縮や乾燥しても、又は抽
出液を活性炭等で脱色して濃縮や乾燥してもよく、いず
れも本発明により製造される胡麻抽出物の効果が損なわ
れることはない。
After the second extraction, the insoluble matter is separated in the same way as the second extraction, and the resulting extract can be directly concentrated and dried, or the extract can be decolorized with activated carbon and concentrated or dried. In either case, the effectiveness of the sesame extract produced according to the present invention is not impaired.

本発明において、油脂類を多く含む原料を使用する場合
には、−回目或いは二回目の抽出後の濃縮途中又は濃縮
後に、溶媒抽出、分離、吸着等の方法で油脂類を除去す
ることが望ましい。また、本発明の基本的操作の性格を
損なわない範囲において、以上説明した操作中に他の種
々の操作を組み入れても差し支えない。
In the present invention, when using raw materials containing a large amount of fats and oils, it is desirable to remove the fats and oils by methods such as solvent extraction, separation, and adsorption during or after the second or second extraction. . Further, various other operations may be incorporated into the operations described above as long as the characteristics of the basic operations of the present invention are not impaired.

本発明は、以上説明したようなエタノール及び/又は水
系における簡便な方法であり、これによって製造される
胡麻抽出物は、単独で、或いは溶液として、又は他の成
分と組み合わせて使用することができ、優れた抗酸化性
等変質防止性能を発揮するのである。
The present invention is a simple method using ethanol and/or water as explained above, and the sesame extract produced by this method can be used alone, as a solution, or in combination with other components. It exhibits excellent anti-oxidation properties and other deterioration prevention properties.

最後に、本発明をより具体的にするだめ、実施例及び得
られた胡麻抽出物の効果について示す。
Finally, in order to make the present invention more specific, Examples and the effects of the obtained sesame extract will be shown.

・実施例1 中国産胡麻種子を圧搾搾油機にて搾油した脱脂胡麻種子
(残油分8.8%)1kgを10/四つロフラスコ(攪
拌器付き)に採り、残油分を除くためn−へキサン4k
gを加えて室温下で4時間攪゛拌抽出した後、スラリー
をヌノチェで濾過して固形分を分離し、室温下で通風乾
燥した。この脱脂胡麻種子の全量を10/四つロフラス
コ(攪拌器付き)に採り、80%(W/w ) xタノ
ール4.5 kg f、室温下に10時間攪拌抽出後、
スラリーをヌソチェで濾過し、抽出液8.92kgを得
だ。この抽出液1 kgをエバポレータに入れ、50℃
でエタノール分を除き、凍結乾燥して抽出物(これを抽
出物Aとする)14gを得た。別に、残りの抽出液29
2 kgを51四つロフラスコ(攪拌器付き)に採り、
減圧下に40〜50℃で濃縮し、固形分42.3%(残
留溶媒中の含水量はぼ100 % )の濃縮液63gを
得、これに再度99%(W/W)エタノール100gを
室温で攪拌しつつ徐々に加え、1時間攪拌抽出した。次
いで、不溶分をヌッチェで戸別して抽出液107gを得
、50℃でエバポレータにてエタノール分を除いた後、
凍結乾燥して本発明による抽出物(これを抽出物Bとす
る)12gを得だ。
・Example 1 1 kg of defatted sesame seeds (residual oil content 8.8%) obtained by extracting oil from Chinese sesame seeds using an oil pressing machine was taken into a 10/4-bottle flask (with a stirrer), and transferred to n- to remove the residual oil. Kisan 4k
After stirring and extracting at room temperature for 4 hours, the slurry was filtered through Nunoche to separate the solid content, and dried under ventilation at room temperature. The entire amount of these defatted sesame seeds was taken into a 10/4 cup flask (with a stirrer), and extracted with 80% (w/w) x 4.5 kg of ethanol at room temperature for 10 hours with stirring.
The slurry was filtered through Nusoche to obtain 8.92 kg of extract. Pour 1 kg of this extract into an evaporator and heat at 50°C.
The ethanol content was removed and lyophilized to obtain 14 g of an extract (this will be referred to as extract A). Separately, remaining extract 29
2 kg was taken into a 51-piece four-loaf flask (with a stirrer),
Concentrate at 40 to 50°C under reduced pressure to obtain 63 g of a concentrated solution with a solid content of 42.3% (water content in the residual solvent is approximately 100%), and add 100 g of 99% (W/W) ethanol to this again at room temperature. The mixture was gradually added while stirring, and the mixture was extracted with stirring for 1 hour. Next, 107 g of the extract was obtained by removing the insoluble content using a Nutsche, and removing the ethanol content using an evaporator at 50°C.
Freeze-drying yielded 12 g of the extract according to the invention (designated as extract B).

ここで得た抽出物Aは褐色、不均一固状であり、水分0
.8%、油分2.7%、全糖量(グルコース標準)63
.1係、窒素含有量111%(タンノ々り質換算69チ
)であった。捷た抽出物Bは黄褐色固状であり、水分0
4チ、窒素含有量0.96係(タンパク質換算6.0%
)であって、水に分散し、油脂に難溶であった。そして
、抽出物Bについてトコフェロール、セザモールの含有
量を測定したとこ口、全+−コフェロールは9ppm、
セザモールは検出されなかった。
The extract A obtained here is brown, heterogeneous solid, and has no water content.
.. 8%, oil content 2.7%, total sugar content (glucose standard) 63
.. 1, the nitrogen content was 111% (69% in terms of tannochlorite). The strained extract B is a yellowish brown solid with 0 water content.
4. Nitrogen content: 0.96% (protein equivalent: 6.0%)
), which was dispersed in water and sparingly soluble in fats and oils. When the content of tocopherol and cezamol was measured for extract B, the total +- copherol was 9 ppm.
Cezamol was not detected.

・実施例2 中国産胡麻種子を圧搾搾油機にて搾油した脱脂胡麻種子
(残油分8.8%)1kgを10を四つロフラスコ(攪
拌器付き)に採り、75kgの蒸留水を加えて室温下に
10時間撹拌抽出後、スラリーをヌノチェで濾過し、抽
出液4.52kgを得た。この抽出液を凍結乾燥して抽
出物(これを抽出物Cとする)705gを得だ。次いで
、この抽出物C30gを500s+を四つロフラスコ(
攪拌器付き)に採り、30gの水に溶解(一部不溶)シ
、室温で攪拌下に99%(W/w )エタノール300
gを徐々に加え、30分間攪拌抽出し、ヌノチェで濾過
して不溶分を除去した。得られた抽出液を50℃にてエ
バポレータでエタノール分を除き、凍結乾燥して本発明
による抽出物(これを抽出物りとする)6.4gを得た
・Example 2 1 kg of defatted sesame seeds (residual oil content 8.8%) obtained by extracting oil from Chinese sesame seeds using an oil press machine was placed in four 10 flasks (with a stirrer), 75 kg of distilled water was added, and the mixture was heated to room temperature. After stirring and extraction for 10 hours, the slurry was filtered through a Nunoche to obtain 4.52 kg of extract. This extract was freeze-dried to obtain 705 g of an extract (designated as extract C). Next, 500s+ of 30g of this extract C was placed in four Lof flasks (
(with a stirrer), dissolve (partially insoluble) in 30 g of water, and add 99% (w/w) ethanol 300 to 99% (w/w) while stirring at room temperature.
g was gradually added, stirred and extracted for 30 minutes, and filtered through Nunoche to remove insoluble matter. The ethanol content of the obtained extract was removed using an evaporator at 50° C., and the extract was freeze-dried to obtain 6.4 g of the extract according to the present invention (this is referred to as the extract).

ここで得だ抽出物Cは褐色固状で、水分1.1%、窒素
含有量8.74%(タンパク質換算28.4%)であっ
た。まだ抽出物りは黄褐色固状で、水分08チ、窒素含
有量122%(タンパク質換算7.6%うであり、水分
散性であった。
Here, Tokuda extract C was a brown solid with a water content of 1.1% and a nitrogen content of 8.74% (28.4% in terms of protein). The extract was still a yellowish brown solid with a water content of 0.8%, a nitrogen content of 122% (7.6% in terms of protein), and water dispersibility.

・実施例3 コロンビア産胡麻種子を圧搾搾油機にて搾油した脱脂胡
麻種子(残油分9.0%)1kgを10/四つロフラス
コ(攪拌器付き)に取り、92 % (W/W)エタノ
ール4.0 kgを加え、室温にて10時間攪拌抽出後
、スラリーをヌノチェで濾過し、抽出g311hgを得
た。この抽出液全量を51四つロフラスコ(攪拌器付き
)に採9、減圧下で40〜50℃にて濃縮して全量を2
27gとし、分液ロートに移して油分を分層させること
により分離除去し、固形分11.0%(残留溶媒中の含
水量651の濃縮液188gを得だ。この濃縮液全量を
工l四つロフラスコNu拌器付き)に採り、室温で攪拌
しつつ99φ(W/w)エタノール400gを徐々に加
え、30分間攪拌抽出を続けた後、不溶分をヌノチェで
p別し、抽出液521gを得だ。
・Example 3 1 kg of defatted sesame seeds (residual oil content 9.0%) obtained by extracting oil from Colombian sesame seeds using an oil pressing machine was placed in a 10/4 flask (with a stirrer), and 92% (W/W) ethanol was added. After adding 4.0 kg and stirring for extraction at room temperature for 10 hours, the slurry was filtered through Nunoche to obtain 311hg of extract. The total amount of this extract was taken into a four-loaf flask (with a stirrer)9, and concentrated under reduced pressure at 40-50°C to reduce the total amount to 2.
27 g, and transferred to a separatory funnel to separate and remove the oil, yielding 188 g of a concentrated solution with a solid content of 11.0% (water content in the residual solvent: 651%). Add 400 g of 99φ (W/w) ethanol gradually while stirring at room temperature, continue stirring and extracting for 30 minutes, separate the insoluble matter with a Nunoche, and add 521 g of the extract. It's a good deal.

この抽出液全量に活性炭10gを加え、室温下で30分
間攪拌処理した後、ヌソチェで濾過し、得うしたp液を
50℃でエバポレータにてエタノール分を除去した後、
凍結乾燥して、本発明による抽出物(これを抽出物Eと
する)10.6gを得だ。
10 g of activated carbon was added to the entire extract, stirred at room temperature for 30 minutes, filtered through Nusoche, and the resulting p solution was heated at 50°C to remove the ethanol content with an evaporator.
After lyophilization, 10.6 g of the extract according to the present invention (designated as extract E) was obtained.

ここで得だ抽出物Eは黄褐色固状で、水分04チ、窒素
含有量0.24%(タンパク質換算15係)であった。
Tokuda extract E was a yellowish brown solid with a water content of 0.4% and a nitrogen content of 0.24% (15 parts in terms of protein).

・比較例1 コロンビア産胡麻種子を圧搾搾油機にて搾油した脱脂胡
麻種子(残油分9.0 % ) 1 kgを10/四つ
ロフラスコ(攪拌器付き)に採り、99%(W/W )
エタノール4.0 kgを加え、室温にて10時間攪拌
抽出後、ヌノチェで濾過し、抽出液3.23kgを得た
。この抽出液全量を減圧下で40〜50℃にてエバポレ
ータにより脱溶媒し、不均一油状の抽出物102gを得
た。次いで、この抽出物全量を1−ヘキサン400 (
lと80%(W/w ) エタノール300gとで分液
した。n−ヘキサン層を乾燥したところ、黄褐色油状物
98gが得られ、これを分析すると、トリグリセライド
(γ−トコフェロール0018%を含む)であった。一
方、エタノール/水層からは褐色の半固状物(これを抽
出物Fとする)2.117が得られた。この抽出物Fは
水分023係、酸価281を示しだ。
・Comparative Example 1 1 kg of defatted sesame seeds (residual oil content 9.0%) obtained by extracting oil from Colombian sesame seeds using an oil presser was taken into a 10/4 flask (with a stirrer), and 99% (W/W) was obtained.
After adding 4.0 kg of ethanol and stirring for extraction at room temperature for 10 hours, the mixture was filtered through Nunoche to obtain 3.23 kg of an extract. The entire amount of this extract was desolvated using an evaporator at 40 to 50° C. under reduced pressure to obtain 102 g of a heterogeneous oily extract. Next, the entire amount of this extract was mixed with 400% of 1-hexane (
1 and 300 g of 80% (w/w) ethanol. When the n-hexane layer was dried, 98 g of a yellow-brown oil was obtained, which was analyzed to be triglyceride (containing 0.018% of γ-tocopherol). On the other hand, from the ethanol/water layer, 2.117 brown semi-solid substances (this was referred to as Extract F) were obtained. This extract F had a water content of 0.23 and an acid value of 281.

・性能実験1 次の配合割合のマヨネーズを製造し、このマヨネーズに
それぞれ、抽出物A−F、dl−α−トコフェロール、
市販天然抗酸化剤(ライオンマコーミノク社製、5P−
10)を添加して、35℃で保存した。所定経口後に、
該マヨネーズ中の油脂分をエチルエーテルで抽出し、常
法でその過酸化物価(ミリ当量/に41)を測定するこ
とにより、マヨネーズ中の油脂分に対する抗酸化性指標
としだ。
・Performance experiment 1 Mayonnaise with the following blending ratio was manufactured, and extracts A-F, dl-α-tocopherol,
Commercially available natural antioxidant (manufactured by Lion Macorminok Co., Ltd., 5P-
10) was added and stored at 35°C. After prescribed oral administration,
The fats and oils in the mayonnaise are extracted with ethyl ether and the peroxide value (milliequivalents/41) is measured using a conventional method, which is used as an antioxidant index for the fats and oils in the mayonnaise.

高度精製胡麻油”     100C1yZ食    
 酢            80肩を卵     黄
           100 g食    塩   
         15g(*1=含有する抗酸化性成
分や色素等を除去するだめ、塩基性アルミナを充填しだ
カラムを通して精製した) 結果を第1表に示す。
Highly refined sesame oil” 100C1yZ food
vinegar 80g egg yolk 100g salt
15g (*1 = Purified through a column packed with basic alumina in order to remove the antioxidant components, pigments, etc. contained) The results are shown in Table 1.

第1表 第1表の結果からも、本発明による抽出物B、DXEは
その他に比べていずれも良好な抗酸化性を有することが
判る。
The results shown in Table 1 also show that both Extract B and DXE according to the present invention have better antioxidant properties than the others.

・性能実験−2 水溶性β−カロチン末(三共社製)を水に溶解希釈し、
β−カロチン6 ppmを含有する水溶液を調整した。
・Performance experiment-2 Water-soluble β-carotene powder (manufactured by Sankyosha) was dissolved and diluted in water.
An aqueous solution containing 6 ppm of β-carotene was prepared.

そして、抽出物A−FXdl−α”□゛′′−トコフエ
ロール販天然抗酸化剤(ライオンマコーミノク社製、5
P−100)を各々用いて、抽出物Aと抽出物Cは1%
水溶液、他は1%エタノール溶液を調整し、各々を第2
表中に記す量で前記β−カロチン溶液に加え、充分に混
合した。この試料50m1を70M/のガラスシリンダ
に移し、密栓放置して、室内分散光下で橙色が完全に認
められなくなる迄の日数を測定し、各々のβ−カロチン
に対する退色防止性指標とした。
Extract A-FXdl-α”□゛′′-tocopherol natural antioxidant (manufactured by Lion Macorminok Co., Ltd., 5
P-100) respectively, extract A and extract C were 1%
Prepare an aqueous solution and a 1% ethanol solution for the other, and add each to the second
The amounts listed in the table were added to the β-carotene solution and mixed thoroughly. 50 ml of this sample was transferred to a 70M glass cylinder, left sealed, and the number of days until the orange color was completely no longer recognized under indoor diffused light was measured, and this was used as an index of antifading property for each β-carotene.

結果を第2表に示す。The results are shown in Table 2.

第2表 第2表の結果からも、本発明による抽出物B、DlEは
その他に比べていずれも良好な退色防止性を有すること
が判る。
From the results shown in Table 2, it can be seen that both extracts B and DlE according to the present invention have better anti-fading properties than the others.

特許出願人   竹本油脂株式会社 代理人 弁理士 入 山 宏 正 特許庁長官 若 杉 和 夫 殿 20発明の名称  胡麻抽出物の製造方法3、補正をす
る者 事件との関係 特許出願人 住 所  愛知県蒲郡市港町2番5号 4、代理人 ・− 住 所  愛知県名古屋市中区栄5丁目21番16号5
゜補正命令の日付   (自発) 6、補正の対象  明細書の特許請求の範囲の欄及び発
明の詳細な説明の欄 7、補正の内容  別紙の通シ フ、補正の内容 (1)明細書第5頁第3行の「・・・水又はエタノール
可溶性」を「・・・水又はエタノール可溶性乃至分散性
」と補正します。
Patent Applicant Takemoto Yushi Co., Ltd. Agent Patent Attorney Hiroshi Iriyama Director of the Patent Office Kazuo Wakasugi 20 Title of Invention Method for Producing Sesame Extract 3, Relationship to the Amendment Case Patent Applicant Address Aichi Prefecture 2-5-4, Minato-cho, Gamagori City, Agent - Address: 5-21-16-5 Sakae, Naka-ku, Nagoya, Aichi Prefecture
゜Date of amendment order (voluntary) 6. Subject of amendment Scope of claims and detailed description of the invention column 7 of the specification Contents of amendment Announcement of attached sheet, Contents of amendment (1) Description No. 5 Correct "...water or ethanol soluble" in the third line of the page to "...water or ethanol soluble or dispersible".

(2)明細書第14頁第3行の「抽出物102g・・・
」を[抽出物62f・・・]と補正します。
(2) “Extract 102g...” on page 14, line 3 of the specification.
" is corrected to [Extract 62f...].

(3)明細書第14頁第6行の「・・・油状物981・
・・」を1・・・油状物58f!・・・」と補正し捷す
(3) On page 14, line 6 of the specification: “...oily substance 981.
``...'' 1...58f of oily substance! "..." he corrected himself.

2、特許請求の範囲 1破砕された胡麻種子100重量部に対し、水単独或い
は5重量%以上の水を含有するエタノール−水混合溶媒
を250重量部以上刀口えて抽出し、不溶分を除去した
後、得られる抽出液を濃縮或いは乾燥して該抽出液が4
0重量部以下且つ残留溶媒中の含水量が50重量係以上
になるようにし、次いでエタノール単独或いはエタノー
ル−水混合溶媒を加え、エタノール:水の重量比が]、
 OO: O〜60:40の範囲の溶媒とし且つ全量が
100重量部以下になる範囲で再度抽出することを特徴
とする胡麻抽出物の製造方法。
2. Claims 1 100 parts by weight of crushed sesame seeds are extracted with water alone or 250 parts by weight or more of an ethanol-water mixed solvent containing 5% by weight or more of water to remove insoluble matter. After that, the obtained extract is concentrated or dried to obtain 4
0 parts by weight or less and the water content in the residual solvent is 50 parts by weight or more, then ethanol alone or a mixed solvent of ethanol and water is added so that the weight ratio of ethanol to water is],
OO: A method for producing a sesame extract, characterized by using a solvent in the range of O to 60:40 and extracting again in a range where the total amount is 100 parts by weight or less.

Claims (1)

【特許請求の範囲】[Claims] 1 破砕された胡麻種子100重量部に対し、水単独或
いは5重量以上の水を含有するエタノール−水混合溶媒
を250重量部以上加えて抽出し、不溶分を除去した後
、得られる抽出液を濃縮或いは乾燥して該抽出液が40
重量部以下且つ残留溶媒中の含水量が50重量係以上に
なるようにし、次いでエタノール単独或いはエタノール
−水混合溶媒を加え、エタノール:水の重量比がZoo
:O〜60°40の範囲の溶媒とし且つ全量が100重
量部以下になる範囲で再度抽出することを特徴とする胡
麻抽出物の製造方法。
1. Extract 100 parts by weight of crushed sesame seeds by adding 250 parts by weight or more of water alone or a mixed solvent of ethanol and water containing 5 weight or more of water, remove insoluble matter, and extract the resulting extract. Concentrate or dry the extract to 40%
The water content in the residual solvent should be 50 parts by weight or less, and then ethanol alone or a mixed solvent of ethanol and water should be added to adjust the weight ratio of ethanol to water to Zoo.
: A method for producing a sesame extract, characterized by using a solvent in the range of 0 to 60°40 and extracting again in a range where the total amount is 100 parts by weight or less.
JP57160640A 1982-09-13 1982-09-13 Preparation of extract of sesame Granted JPS5948064A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57160640A JPS5948064A (en) 1982-09-13 1982-09-13 Preparation of extract of sesame

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57160640A JPS5948064A (en) 1982-09-13 1982-09-13 Preparation of extract of sesame

Publications (2)

Publication Number Publication Date
JPS5948064A true JPS5948064A (en) 1984-03-19
JPS6126342B2 JPS6126342B2 (en) 1986-06-20

Family

ID=15719297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57160640A Granted JPS5948064A (en) 1982-09-13 1982-09-13 Preparation of extract of sesame

Country Status (1)

Country Link
JP (1) JPS5948064A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100414185B1 (en) * 2000-10-09 2004-01-07 대한민국 A method for preparing lignan powder, lignan powder prepared thereby and a method for preventing oxidization of meat and meat products by adding the lignan powder thereto

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0426900Y2 (en) * 1986-08-18 1992-06-29

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100414185B1 (en) * 2000-10-09 2004-01-07 대한민국 A method for preparing lignan powder, lignan powder prepared thereby and a method for preventing oxidization of meat and meat products by adding the lignan powder thereto

Also Published As

Publication number Publication date
JPS6126342B2 (en) 1986-06-20

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