JPH0873396A - Lipid having high natural menaquinone-7 content - Google Patents
Lipid having high natural menaquinone-7 contentInfo
- Publication number
- JPH0873396A JPH0873396A JP7196007A JP19600795A JPH0873396A JP H0873396 A JPH0873396 A JP H0873396A JP 7196007 A JP7196007 A JP 7196007A JP 19600795 A JP19600795 A JP 19600795A JP H0873396 A JPH0873396 A JP H0873396A
- Authority
- JP
- Japan
- Prior art keywords
- natural
- lipid
- solvent
- menaquinone
- content
- 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
Links
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は納豆菌に代表される
枯草菌で発酵せしめた食品素材を原料として得られる天
然メナキノン−7高含量の脂質およびその製造方法、並
びに該脂質を主成分とする骨粗鬆症の予防または/かつ
治療用組成物に関するものである。TECHNICAL FIELD The present invention relates to a lipid containing a high content of natural menaquinone-7 obtained from a food material fermented with Bacillus subtilis typified by Bacillus natto, a method for producing the lipid, and a main component of the lipid. The present invention relates to a composition for preventing or / and treating osteoporosis.
【0002】[0002]
【従来の技術】ビタミンKは古くから血液凝固に関与す
るビタミンとして知られ、ビタミンK欠乏性出血症の治
療に医薬品として合成ビタミンK1 およびK2 が用いら
れ、予防に食品として天然ビタミンK1 濃縮物が利用さ
れている。骨粗鬆症は、老化、疾病などの原因によって
起こる、骨がもろくなる病態で、骨折したり、激しい痛
みなどを伴い、老人医療の面から大きな社会問題となり
つつある。骨粗鬆症の治療、予防には、主にカルシウ
ム、ビタミンD類が医薬品あるいは食品として利用され
ているが、最近になって骨粗鬆症の治療、予防にビタミ
ンKが単独、あるいは既知の有効物質との併用で有効で
あることが見いだされた。出血症の治療、予防に必要な
ビタミンKは極めて微量(一日当たりμgオーダー)で
あるが、骨粗鬆症の治療、予防には一日当たり数〜数十
mgのビタミンKを必要とする。2. Description of the Related Art Vitamin K has long been known as a vitamin involved in blood coagulation. Synthetic vitamins K 1 and K 2 are used as medicines for the treatment of vitamin K deficiency hemorrhage, and natural vitamin K 1 is used as food for prevention. A concentrate is used. Osteoporosis is a pathological condition in which bones become brittle due to aging, diseases, and the like, and is becoming a major social problem in terms of medical care for the elderly, with fractures and severe pain. Calcium and vitamin D are mainly used as medicines or foods for the treatment and prevention of osteoporosis. Recently, vitamin K alone or in combination with a known active substance has been used for the treatment and prevention of osteoporosis. It was found to be effective. Vitamin K required for the treatment and prevention of hemorrhage is extremely small (on the order of μg per day), but for the treatment and prevention of osteoporosis, it is several to several tens per day.
You need mg vitamin K.
【0003】ビタミンK類の中で、自然界に存在するの
はビタミンK1 およびK2 群のみである。K1 は主に植
物によって合成される。K2 群の中には側鎖長の違いに
よりメナキノン(MK)−1〜14までが知られてお
り、MK−4は主に動物体内の腸内細菌によって合成さ
れ、MK−7は主に納豆菌によって合成される。食品中
では、K1 は特に緑色野菜、植物油、海藻等に多く含ま
れており、K2 の代表的な物質であるMK−7は納豆に
多く含まれている。主な食品あるいは食品素材中のビタ
ミンK含量は、海藻・海苔・茶葉などにビタミンK1 が
数十ppm 、大豆油・ほうれん草・ブロッコリなどにビタ
ミンK1 が数ppm 、納豆中にMK−7が数〜十数ppm で
ある。大豆油や納豆の原料である大豆中には1ppm 以下
のビタミンK1 しか含有されていない。Of the vitamin Ks, only the vitamins K 1 and K 2 are naturally present. K 1 is mainly synthesized by plants. Menaquinone (MK) -1 to 14 are known in the K 2 group due to the difference in side chain length, MK-4 is mainly synthesized by intestinal bacteria in the animal body, and MK-7 is mainly Synthesized by Bacillus natto. Among foods, K 1 is particularly abundant in green vegetables, vegetable oils, seaweed, etc., and MK-7, which is a typical substance of K 2 , is abundant in natto. Vitamin K content of the main food or in food materials, vitamin K 1 is a few tens of ppm, such as in seaweed, laver, brown leaf, vitamin K 1 is a few ppm to, such as soybean oil, spinach, broccoli, MK-7 in natto It is several to ten and several ppm. Soybean oil or soybean, which is a raw material of natto, contains only 1 ppm or less of vitamin K 1 .
【0004】[0004]
【発明が解決しようとする課題】市販の食品から骨粗鬆
症に有効な量のビタミンKを摂取する場合、仮にビタミ
ンKを1ppm 含有する食品あるいは食品素材より一日1
0mgのビタミンKを摂取しようとすると、一日に10kg
もの量を食する必要があり不可能である。十数ppm 含有
する納豆でも一日数百gを食さなくてはならず、嗜好
上、これだけの量を毎日食することは困難である。市販
の、出血症予防のために調製粉乳に添加している天然ビ
タミンK1 濃縮物は高価であるため、大量のビタミンK
1 を摂取するには価格面で困難である。一方、医薬品の
合成ビタミンKは食品に使用することはできない。When ingesting an effective amount of vitamin K for osteoporosis from a commercially available food, it is assumed that 1 day a day from a food or food material containing 1 ppm of vitamin K.
If you try to take 0 mg of vitamin K, 10 kg per day
It is impossible because it is necessary to eat a large amount. Even natto containing a few dozen ppm must eat several hundred g per day, and it is difficult to eat such an amount every day because of taste. Since a large amount of natural vitamin K 1 concentrate that is added to powdered milk formula for preventing hemorrhage on the market is expensive, a large amount of vitamin K is required.
It is difficult to take 1 in terms of price. On the other hand, synthetic vitamin K, which is a drug, cannot be used in foods.
【0005】天然MK−7は、自然界には極微量しか存
在しないため、単離が非常に困難とされており、これま
で、MK−7高含量の脂質を調製した例は知られていな
い。蛋白質との複合体の形で存在するMK−7を水によ
る抽出によって分離した例はあるが、MK−7の一部し
か複合体で存在していないので抽出効率に問題がある。
納豆から、ステロールを主成分とする組成物を抽出した
例もあるが、ステロール含量を高めるためにケン化反応
を必須としており、使用する強アルカリによってMK−
7は分解してしまうため、得られた組成物中にMK−7
はほとんど含有されない。[0005] Natural MK-7 is extremely difficult to isolate because it exists in the natural world in a very small amount, and thus far no examples of preparing lipids with a high MK-7 content have been known. Although there is an example in which MK-7 existing in the form of a complex with a protein is separated by extraction with water, there is a problem in extraction efficiency because only a part of MK-7 is present in the complex.
There is also an example in which a composition containing sterol as a main component is extracted from natto, but a saponification reaction is indispensable to increase the sterol content, and MK-
7 decomposes, so MK-7 in the obtained composition
Is hardly contained.
【0006】[0006]
【課題を解決するための手段】本発明の目的は、通常の
食品からは充分な量の摂取ができない、または摂取困難
な天然ビタミンK、特に納豆菌に代表される可食の枯草
菌によって作り出された天然MK−7を、食品あるいは
補助食品として簡単に日常的摂取ができるようにした天
然MK−7高含量の濃縮脂質、およびそれを主成分とす
る食品あるいは補助食品を提供することにある。The object of the present invention is produced by natural vitamin K which cannot be ingested in a sufficient amount from ordinary foods or is difficult to ingest, particularly edible Bacillus subtilis represented by Bacillus natto. To provide a concentrated lipid having a high content of natural MK-7, which allows the natural MK-7 to be easily ingested daily as a food or a supplement, and a food or supplement containing the same as a main component. .
【0007】本発明者らは、上記の目的を達成すべく鋭
意研究を重ねた結果、枯草菌で発酵した食品素材より脂
質を取り出すか、あるいは抽出または抽出、精製するこ
とによって天然MK−7高含量脂質を得ることができる
ことを見出して本発明を完成した。本発明において、脂
質の原料となるものは、納豆菌に代表される枯草菌を繁
殖させ発酵させることができるものであれば使用できる
が、発酵物より取り出した脂質を食用に供することから
食品素材が好ましい。食品素材は、一般食品の材料とな
るものの他に、それらの加工過程で発生する粕や煮汁な
どの副産物を用いてもよい。一般食品としては、特に大
豆などの穀類が好ましい。上記の他にも、食することが
可能で枯草菌が繁殖できるものであれば特に限定するも
のでない。The inventors of the present invention have conducted extensive studies to achieve the above object, and as a result, extracted natural lipids from the food material fermented with Bacillus subtilis or extracted or extracted and purified the natural MK-7 The present invention has been completed by finding that a lipid content can be obtained. In the present invention, the raw material for the lipid can be used as long as it can ferment and ferment Bacillus subtilis typified by Bacillus natto, but since the lipid taken out from the fermented product is edible, it is a food material. Is preferred. As the food material, by-products such as lees and broth produced during the processing thereof may be used in addition to the materials for general foods. As the general food, grains such as soybean are particularly preferable. Other than the above, it is not particularly limited as long as it can be eaten and can reproduce Bacillus subtilis.
【0008】接種する枯草菌としては、上記素材と同様
な理由から可食の枯草菌が好ましい。可食の枯草菌とし
ては、納豆菌が最も一般的である。市販の納豆菌が使用
できるが、その中でも天然MK−7産生能力の高いもの
が望ましい。また、人為的に天然MK−7産生能力を高
めたものも使用できる。発酵方法は、一般的に知られて
いる納豆の発酵方法の他に液体培養などの公知の発酵方
法を用いてもよい。通常、納豆の発酵は36〜39℃で
15〜20時間かけて行われるが、さらに42℃以上の
温度で、48時間以上の長時間発酵させることによっ
て、脂質中の天然MK−7含量を高めることができる。As the Bacillus subtilis to be inoculated, edible Bacillus subtilis is preferable for the same reason as the above material. Bacillus subtilis is the most common edible Bacillus subtilis. Commercially available Bacillus natto can be used, and among them, those having a high natural MK-7 producing ability are preferable. In addition, it is also possible to use those artificially enhanced in natural MK-7 production ability. As the fermentation method, in addition to the generally known fermentation method for natto, a known fermentation method such as liquid culture may be used. Usually, the fermentation of natto is carried out at 36 to 39 ° C for 15 to 20 hours, but the fermentation of the fermented soybeans at a temperature of 42 ° C or more for a long time of 48 hours or more enhances the content of natural MK-7 in the lipid. be able to.
【0009】取り出す方法は抽出、圧搾、遠心分離など
物性の相違を利用して分ける方法を選択できるが、特に
抽出法が効果的である。抽出方法は、発酵物に対して最
も効果的な方法を選択すればよく、特に限定されるもの
ではないが、発酵物の固形分量が多ければ固−液抽出法
が、少なければ液−液抽出法が効果的である。固−液抽
出法を選択する場合、発酵物は固体でも多量の水分を含
有しているので、あらかじめ水分含量を測定して、その
水分含量に対して等倍〜10倍量の親水性有機溶媒を混
合するか、減圧下で100℃以下の温度で加熱するかし
て水を除去してから、親油性有機溶媒を等倍〜10倍量
添加して、粉砕・抽出すると抽出効率が向上する。As a method of taking out, a method of separating by utilizing differences in physical properties such as extraction, squeezing and centrifugation can be selected, and the extraction method is particularly effective. The extraction method may be selected the most effective method for the fermented product and is not particularly limited, but if the solid content of the fermented product is high, the solid-liquid extraction method is used, and if the solid content is low, the liquid-liquid extraction is used. The law is effective. When the solid-liquid extraction method is selected, the fermented product contains a large amount of water even if it is a solid. Therefore, the water content is measured in advance, and the hydrophilic organic solvent has an equal to 10 times the water content. Water is removed by mixing or heating at a temperature of 100 ° C. or lower under reduced pressure, and then a lipophilic organic solvent is added in an equal to 10 times amount, and pulverization / extraction improves extraction efficiency. .
【0010】親水性有機溶媒と混合して脱水を行う場合
は、親水性溶媒−水混液を分離・除去してから脂質を抽
出してもまた除去せずに抽出してもよい。親水性溶媒−
水混液を除去してから抽出する場合は、分離した親水性
溶媒−水混液を、親油性有機溶媒を用いて更に脂質分を
抽出するとよい。脱水後の発酵物を粉砕し、抽出した
後、ろ過してろ液の親油性有機溶媒層を分取後、減圧下
で溶媒を留去すると抽出脂質が得られる。When dehydration is carried out by mixing with a hydrophilic organic solvent, lipid may be extracted after separating / removing the hydrophilic solvent-water mixture, or may be extracted without being removed. Hydrophilic solvent-
When the extraction is performed after removing the water mixture, the separated hydrophilic solvent-water mixture may be further extracted with a lipophilic organic solvent to extract the lipid component. The dehydrated fermented product is crushed, extracted, filtered, and the lipophilic organic solvent layer of the filtrate is collected, and then the solvent is distilled off under reduced pressure to obtain an extracted lipid.
【0011】液−液抽出法では、水を除去せずに抽出を
行うことができるが、水に対して親和性の低い溶媒か混
合溶媒を選択して、抽出時に二層に分離させる必要があ
る。発酵液に対して1/10〜10倍量の水との親和性
の低い溶媒か混合溶媒を発酵液と混合後、静置、または
加速度を与え強制的に二層を分離して親油性有機溶媒層
を分取後、減圧下で溶媒を留去すると抽出脂質が得られ
る。残った水層に同様の操作を繰り返すと一層効果的で
ある。In the liquid-liquid extraction method, extraction can be carried out without removing water, but it is necessary to select a solvent or a mixed solvent having a low affinity for water to separate the two layers at the time of extraction. is there. After mixing a solvent or a mixed solvent with a low affinity for water that is 1/10 to 10 times the amount of the fermentation liquor with the fermentation liquor, the mixture is allowed to stand, or acceleration is applied to forcibly separate the two layers and lipophilic organic After separating the solvent layer, the solvent is distilled off under reduced pressure to obtain an extracted lipid. It is more effective to repeat the same operation for the remaining water layer.
【0012】有機溶媒としては、炭素数1〜10の炭化
水素あるいはアルコール、エーテル、エステル、ケトン
の群から選ばれる単独あるいは2種以上の混合物が使用
できる。抽出法は、固−液、液−液共にバッチ式でも連
続式でもよい。抽出温度は、溶媒の沸点以下であれば使
用できるが、天然MK−7の化学的分解を抑えるために
は室温〜100℃程度の温度が望ましい。As the organic solvent, a hydrocarbon having 1 to 10 carbon atoms or a mixture of two or more selected from the group consisting of alcohols, ethers, esters and ketones can be used. The extraction method may be a batch type or a continuous type for both solid-liquid and liquid-liquid. The extraction temperature can be used as long as it is not higher than the boiling point of the solvent, but a temperature of about room temperature to 100 ° C. is desirable in order to suppress chemical decomposition of natural MK-7.
【0013】以上の抽出操作のみによっても、得られた
抽出脂質中の天然MK−7含有量は200ppm 〜1%程
度にまで高まる。このとき、脂質中に含有されるMK−
7以外の物質は、油脂、ステロールおよびその誘導体、
トコフェロール、リン脂質、炭化水素等である。Only by the above extraction operation, the content of natural MK-7 in the extracted lipid obtained is increased to about 200 ppm to 1%. At this time, MK- contained in the lipid
Substances other than 7 include fats and oils, sterols and their derivatives,
Examples include tocopherols, phospholipids, hydrocarbons and the like.
【0014】より高含有量の脂質を得るためには、さら
に精製処理を施す必要がある。精製方法としては、溶媒
分別、吸着分別、蒸留、クロマトグラフィー、膜分離の
操作を単独もしくはそれらを2種以上複合した方法が効
果的であるが、油脂中の脂質精製法として一般的なアル
カリ精製法は、使用する強アルカリによってMK−7が
分解してしまうため好ましくない。溶媒分別法には、次
の二種の方法がある。上記の抽出溶媒の範囲の溶媒もし
くはその混合物で互いに混ざり合わない二種の溶媒を選
択し、そのいずれか一方あるいは両方に抽出脂質を溶解
し、二液相間でバッチまたは連続で混合−分離を繰り返
し行うことによって、天然MK−7の分配率の高い溶媒
層に天然MK−7を濃縮する。それを分取して減圧下で
溶媒を留去して天然MK−7高含量脂質を得る。溶媒の
混合比率は、一方の溶媒1倍量に対して、他方の溶媒を
1/5〜5倍量とすることが望ましい。別法として、抽
出脂質1倍量に対して1/2〜10倍量の、上記の抽出
溶媒の範囲の溶媒もしくはその混合物に抽出脂質を加熱
溶解した後に、冷却して生成したステロール類を主成分
とする不溶物を、ろ過、遠心分離等の方法により除去す
ることによって、天然MK−7高含量の脂質を得る。In order to obtain a higher content of lipid, it is necessary to carry out further purification treatment. As a purification method, a solvent fractionation, an adsorption fractionation, a distillation, a chromatography, a membrane separation operation alone or a combination of two or more thereof is effective, but a general alkali purification as a lipid purification method in fats and oils. The method is not preferable because MK-7 is decomposed by the strong alkali used. There are the following two types of solvent fractionation methods. Two solvents that are immiscible with each other are selected in the above-mentioned extraction solvent range or a mixture thereof, and the extracted lipid is dissolved in either one or both of them, and mixed or separated in batch or continuously between the two liquid phases. By repeating the process, the natural MK-7 is concentrated in the solvent layer having a high distribution rate of the natural MK-7. It is separated and the solvent is distilled off under reduced pressure to obtain a natural MK-7-rich lipid. The mixing ratio of the solvent is preferably 1/5 to 5 times the amount of the other solvent with respect to 1 time of the one solvent. Alternatively, the sterols mainly produced by heating and dissolving the extracted lipid in a solvent in the range of the above-mentioned extraction solvent or a mixture thereof in an amount of 1/2 to 10 times the amount of the extracted lipid are mainly used. The insoluble matter as a component is removed by a method such as filtration or centrifugation to obtain a lipid having a high content of natural MK-7.
【0015】吸着分別法は、MK−7が炭素系吸着剤に
選択的に吸着される性質を利用して、吸着・溶離を行う
方法である。抽出脂質の有機溶媒溶液に活性炭を添加・
混合するか、活性炭を詰めたカラムに抽出脂質の有機溶
媒溶液を通液するかして、活性炭にMK−7を吸着せし
めた後、有機溶媒で活性炭を洗浄して不純物を洗い流
し、有機溶媒でMK−7を溶離して、天然MK−7高含
量の脂質を得る。ここで使用する有機溶媒は、上記の抽
出溶媒の範囲の溶媒もしくはその混合物であるが、吸着
・洗浄には溶離作用の弱い溶媒、主にアルコール類を、
溶離には溶離作用の強い溶媒、主に炭化水素類を使用す
ることによって、より効率的に濃縮を行うことができ
る。The adsorption fractionation method is a method of adsorbing and eluting by utilizing the property that MK-7 is selectively adsorbed by a carbon-based adsorbent. Activated carbon was added to the organic solvent solution of the extracted lipid.
After mixing or passing a solution of the extracted lipid in an organic solvent through a column packed with activated carbon to adsorb MK-7 on the activated carbon, wash the activated carbon with the organic solvent to wash away impurities, and then wash with an organic solvent. Elution of MK-7 gives a lipid with a high content of natural MK-7. The organic solvent used here is a solvent in the above extraction solvent range or a mixture thereof, but a solvent having a weak elution action for adsorption / washing, mainly alcohols,
By using a solvent having a strong elution action, mainly hydrocarbons, elution can be performed more efficiently.
【0016】蒸留法は、天然MK−7が高沸点かつ高温
で分解する物質であることから、高真空蒸留である分子
蒸留法または水蒸気蒸留法が効果的である。両方法と
も、蒸発対象物の蒸気圧を小さくして、高沸点の物質で
も低い温度で蒸発させることができる。これらの蒸留法
は、バッチ式でも連続式でもよい。この方法を適用する
ことによって得られた天然MK−7高含量の脂質は、溶
媒の残留もなく、無臭であるためそのまま食用に供する
ことができる。分子蒸留法では、5Pa以下の圧力で20
0℃〜300℃の温度範囲で、抽出脂質を分子蒸留装置
に付し、段階的温度にて蒸発留分を分取することによっ
て天然MK−7高含量の脂質を得る。水蒸気蒸留法で
は、1kPa 以下の圧力で200〜350℃の温度範囲
で、水または水蒸気を導入しながら蒸留を行い、段階的
温度にて蒸発留分を分取することによって天然MK−7
高含量の脂質を得る。As the distillation method, since natural MK-7 is a substance that has a high boiling point and decomposes at high temperatures, the molecular distillation method or steam distillation method, which is high vacuum distillation, is effective. In both methods, it is possible to reduce the vapor pressure of the object to be vaporized so that even a substance having a high boiling point can be vaporized at a low temperature. These distillation methods may be batch type or continuous type. The lipid with a high content of natural MK-7 obtained by applying this method has no solvent remaining and is odorless, and thus can be directly used for food. In the molecular distillation method, 20 at a pressure of 5 Pa or less
The extracted lipids are subjected to a molecular distillation apparatus in a temperature range of 0 ° C to 300 ° C, and the evaporation fraction is collected at a stepwise temperature to obtain a lipid having a high content of natural MK-7. In the steam distillation method, distillation is carried out at a pressure of 1 kPa or less at a temperature range of 200 to 350 ° C. while introducing water or steam, and an evaporation fraction is collected at a stepwise temperature to obtain a natural MK-7.
A high content of lipids is obtained.
【0017】クロマトグラフィー法は、カラムクロマト
グラフィー法が効果的である。カラムに充填する固定相
は、市販のクロマトグラフィー用充填剤でよい。実用
上、シリカゲルベースの吸着剤もしくは有機ポリマーを
骨格に持った合成吸着剤が望ましい。移動相は、上記の
抽出溶媒の範囲の溶媒もしくはその混合物から選択す
る。以上の精製方法を、単独もしくはそれらを複合して
行うことによって、天然MK−7高含量脂質を得ること
ができる。このときのMK−7含有量は1%以上であ
る。精製を重ねることによってほぼ100%のものも調
製できる。蒸留して得られた天然MK−7高含量脂質に
は脂質以外のものとして、若干量の溶媒が残留している
と共に、発酵物由来の臭気も残留している場合がある。
これらの両方を完全に除去するためには、最後に100
〜250℃にて水蒸気蒸留を行うとよい。水蒸気蒸留
は、流動性がないと適用が困難であるため、溶媒留去時
にペースト状あるいは固体になる場合は、1/2〜5倍
量の植物油に溶解してから水蒸気蒸留処理を行う。As the chromatographic method, a column chromatographic method is effective. The stationary phase packed in the column may be a commercially available packing material for chromatography. Practically, a silica gel-based adsorbent or a synthetic adsorbent having an organic polymer in the skeleton is desirable. The mobile phase is selected from solvents in the above extraction solvent range or mixtures thereof. A natural MK-7-rich lipid can be obtained by performing the above purification methods alone or in combination. At this time, the MK-7 content is 1% or more. Almost 100% can be prepared by repeating purification. The natural MK-7-rich lipid obtained by distillation may contain a small amount of solvent as a substance other than the lipid and also an odor derived from the fermentation product.
To get rid of both of these completely
Steam distillation may be performed at a temperature of up to 250 ° C. Steam distillation is difficult to apply unless it has fluidity. Therefore, when it becomes a paste or a solid when the solvent is distilled off, it is dissolved in 1/2 to 5 times the amount of vegetable oil before steam distillation treatment.
【0018】[0018]
【発明の効果】本発明により得られた天然MK−7高含
量脂質は、原料が天然物であり、かつ食することのでき
るものであることから、出血症はもちろん骨粗鬆症の予
防のために、食品あるいは補助食品として安全性が高く
簡易に日常的摂取ができる。また、この脂質は無味・無
臭であることから、嗜好上の問題もなく、様々な形態の
食品に応用することが可能である。The natural MK-7-rich lipid obtained according to the present invention is a natural material and is edible, so that it is effective for preventing not only hemorrhage but also osteoporosis. It is highly safe as a food or supplement and can be easily taken on a daily basis. Further, since this lipid is tasteless and odorless, it can be applied to various forms of food without any problem in taste.
【0019】[0019]
【発明の実施の形態】次に実施例によって本発明を詳し
く説明するが、本発明はこれらに限定されるものではな
い。なお、以下の実施例においてMK−7含量は(財)
日本食品分析センターの高速液体クロマトグラフ法に準
じて測定した値を、その他の分析値は公定法に準じて測
定した値を示す。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will now be described in detail by way of examples, which should not be construed as limiting the invention thereto. In the following examples, the MK-7 content is (goods)
The values measured according to the high performance liquid chromatograph method of the Japan Food Analysis Center, and the other analysis values are the values measured according to the official method.
【0020】実施例1 室温下、市販の挽き割り納豆(MK−7含量17.2pp
m ;水分57.7%)3kgにイソプロピルアルコール
2.3Lを加えて粉砕後、n−ヘキサン4.6Lを加え
て再度粉砕した。全量をろ過した後に、ろ液を静置して
分離したn−ヘキサン層(上層)を分取した。上層は
5.2Lであった。上層の溶媒を2kPa ,60℃で留去
し、153gの残渣を得た。この残渣を3hPa ,170
℃,1.5g水蒸気/時間で60分間脱臭を行って、黄
色、無味、無臭、油状の脂質()144gを得た。こ
の脂質には、MK−7 351ppm ,トコフェロール
135ppm が含有されており、TLC(薄層クロマトグ
ラフィー)で観察したところ大部分はトリグリセライド
で微量のステロールおよびその誘導体、リン脂質、炭化
水素類がみられた。この脂質の酸価は1.2、過酸化物
価は0.6であった。MK−7の回収Example 1 Commercially available ground natto (MK-7 content 17.2 pp at room temperature)
2.3 L of isopropyl alcohol was added to 3 kg of m; water content 57.7%) and pulverized, and then 4.6 L of n-hexane was added and pulverized again. After filtering the whole amount, the n-hexane layer (upper layer) separated by allowing the filtrate to stand was separated. The upper layer was 5.2L. The upper layer solvent was distilled off at 2 kPa and 60 ° C. to obtain 153 g of residue. The residue is 3 hPa, 170
The mixture was deodorized for 60 minutes at 1.5 ° C steam / hour at 1.5 ° C to obtain 144 g of a yellow, tasteless, odorless and oily lipid (). This lipid contains MK-7 351 ppm, tocopherol
When it was observed by TLC (thin layer chromatography), most of it was triglyceride and trace amounts of sterols and their derivatives, phospholipids and hydrocarbons were found. This lipid had an acid value of 1.2 and a peroxide value of 0.6. Recovery of MK-7
【0021】実施例2 納豆製造時に副生成する大豆煮汁に納豆菌を接種し、納
豆の製造と同じ条件で培養したもの(MK−7含量1
0.8ppm )10kgにジエチルエーテル10Lを加えて
震とう後、静置して分離したジエチルエーテル層(上
層)を分取した。上層の溶媒を2kPa ,60℃で留去
し、7.9gの残渣を得た。この残渣を5hPa,180
℃,0.08g水蒸気/時間で60分間脱臭を行って、
黄色、無味、無臭、油状の脂質()7.2gを得た。
この脂質には、MK−7 1.4%,トコフェロール
85ppm が含有されており、TLCで観察したところ上
記の他にトリグリセライド、ステロールおよびその誘導
体、リン脂質、炭化水素類がみられた。この脂質の酸価
は0.8、過酸化物価は0.2であった。MK−7の回
収率は93%であった。Example 2 A soybean juice by-produced during the production of natto was inoculated with the natto bacterium and cultured under the same conditions as in the production of natto (MK-7 content 1
After 10 L of diethyl ether was added to 10 kg of 0.8 ppm) and shaken, the diethyl ether layer (upper layer) separated by standing was separated. The upper layer solvent was distilled off at 2 kPa and 60 ° C. to obtain 7.9 g of residue. This residue is 5hPa, 180
Deodorize at 0.08g steam / hour for 60 minutes,
7.2 g of oily lipid () which was yellow, tasteless, odorless and oily was obtained.
This lipid contains MK-7 1.4%, tocopherol
When it was observed by TLC, triglyceride, sterols and their derivatives, phospholipids and hydrocarbons were found in addition to the above. The lipid had an acid value of 0.8 and a peroxide value of 0.2. The recovery rate of MK-7 was 93%.
【0022】実施例3 市販の納豆(MK−7含量8.5ppm )10Kgを80℃
で24時間減圧乾燥して乾燥物4.75kgを得た。乾燥
物の温度が下がらない内に末広鉄工所製2軸エクストル
ーダーに付し、315gの粗油を得た。80℃で粗油に
温水15mlを添加,攪拌し、遠心分離後上層の油層を分
け取った。さらに20%水酸化ナトリウム水溶液6mlを
添加,攪拌し、遠心分離後上層の油層を分け取った。油
層を真空乾燥後、100℃で活性白土15gを添加し,
攪拌,ろ過した。ろ液を3hPa ,180℃,3g水蒸気
/時間で60分間脱臭を行って、黄色、無味、無臭、油
状の脂質296gを得た。この脂質には、MK−7 1
72ppm ,トコフェロール 752ppm が含有されてお
り、TLCで観察したところ大部分はトリグリセライド
で微量のステロールおよびその誘導体、リン脂質、炭化
水素類がみられた。この脂質の酸価は0.2、過酸化物
価は0.1であった。MK−7の回収率は60%であっ
た。Example 3 10 kg of commercially available natto (MK-7 content 8.5 ppm) was added at 80 ° C.
After vacuum drying for 24 hours, 4.75 kg of a dried product was obtained. While the temperature of the dried product did not decrease, it was attached to a twin-screw extruder manufactured by Suehiro Iron Works to obtain 315 g of crude oil. 15 mL of warm water was added to the crude oil at 80 ° C., the mixture was stirred, and after centrifugation, the upper oil layer was separated. Further, 6 ml of 20% aqueous sodium hydroxide solution was added and stirred, and after centrifugation, the upper oil layer was separated. After vacuum drying the oil layer, add 15 g of activated clay at 100 ° C,
It was stirred and filtered. The filtrate was deodorized at 3 hPa, 180 ° C., 3 g steam / hour for 60 minutes to obtain 296 g of a yellow, tasteless, odorless and oily lipid. This lipid contains MK-7 1
It contained 72 ppm and 752 ppm of tocopherol, and as a result of observation by TLC, most of it was triglyceride, and trace amounts of sterols and their derivatives, phospholipids, and hydrocarbons were found. This lipid had an acid value of 0.2 and a peroxide value of 0.1. The recovery rate of MK-7 was 60%.
【0023】実施例4 上記実施例1で得られた脂質()50gを流下膜式分
子蒸留装置に付した。3Paの圧力で200℃から280
℃まで10℃刻みで昇温した。230℃〜280℃まで
に留出した蒸発物を分取して、黄褐色、無味、無臭、ペ
ースト状の脂質10.3gを得た。この脂質には、MK
−7 1560ppm 、トコフェロール 163ppm が含
有されており、TLCで観察したところ上記の他にトリ
グリセライド、ステロールおよびその誘導体、炭化水素
類がみられた。この脂質の酸価は0、過酸化物価は0.
1であった。MK−7の回収率は92%であった。Example 4 50 g of the lipid () obtained in Example 1 above was placed in a falling film type molecular distillation apparatus. 200 ° C to 280 at a pressure of 3Pa
The temperature was raised to 10 ° C in steps of 10 ° C. The evaporate distilled off at 230 ° C to 280 ° C was collected to obtain 10.3 g of a yellowish brown, tasteless, odorless and pasty lipid. This lipid contains MK
-7 1560 ppm and tocopherol 163 ppm were contained, and when observed by TLC, triglyceride, sterol and its derivative, and hydrocarbons were found in addition to the above. This lipid has an acid value of 0 and a peroxide value of 0.
It was 1. The recovery rate of MK-7 was 92%.
【0024】実施例5 市販の顆粒状活性炭50gをイソプロピルアルコールで
充填したカラムに、上記実施例1で得られた脂質()
50gをイソプロピルアルコール150mlに溶解した溶
液を、40℃、空間速度(SV)1.0で通液してMK
−7を吸着せしめた。同様の温度および流速でイソプロ
ピルアルコール1Lを通液してカラムを洗浄した後に、
トルエン500mlを通液してカラムから流出した液の5
0〜500mlの画分を分取した。この画分を2kPa ,6
0℃で溶媒留去し、4.5gの残渣を得た。この残渣に
9mlのアセトンを加えて50℃で溶解後、−20℃で1
時間冷却して、生成した沈殿物をろ別した。ろ液を2kP
a ,60℃で溶媒留去し、3.9gの残渣を得た。この
残渣に大豆油3gを加えて、3hPa ,180℃,0.0
7g水蒸気/時間で60分間脱臭を行って、黄色、無
味、無臭、油状の脂質6.8gを得た。この脂質には、
MK−7 2200ppm ,トコフェロール 12ppm が
含有されており、TLCで観察したところ大部分はトリ
グリセライドで微量のステロールおよびその誘導体、炭
化水素類がみられた。この脂質の酸価は1.5、過酸化
物価は1.8であった。MK−7の回収率は85%であ
った。Example 5 The lipid () obtained in Example 1 above was placed in a column packed with 50 g of commercially available granular activated carbon in isopropyl alcohol.
A solution prepared by dissolving 50 g in 150 ml of isopropyl alcohol was passed at 40 ° C. and a space velocity (SV) of 1.0 to give MK.
-7 was adsorbed. After washing 1 L of isopropyl alcohol at the same temperature and flow rate to wash the column,
5 of the liquid flowing out of the column after passing 500 ml of toluene
Fractions of 0-500 ml were collected. This fraction is 2kPa, 6
The solvent was distilled off at 0 ° C. to obtain 4.5 g of residue. To this residue was added 9 ml of acetone and dissolved at 50 ° C, then at -20 ° C for 1 hour.
After cooling for an hour, the formed precipitate was filtered off. 2kP of filtrate
The solvent was distilled off at a temperature of 60 ° C. to obtain a residue of 3.9 g. To this residue, add 3 g of soybean oil, add 3 hPa, 180 ℃, 0.0
Deodorization was performed for 60 minutes with 7 g steam / hour to obtain 6.8 g of a yellow, tasteless, odorless and oily lipid. In this lipid,
It contained 2200 ppm of MK-7 and 12 ppm of tocopherol, and as a result of TLC observation, most of the triglyceride was found to contain trace amounts of sterols and their derivatives and hydrocarbons. This lipid had an acid value of 1.5 and a peroxide value of 1.8. The recovery rate of MK-7 was 85%.
【0025】実施例6 上記実施例2で得られた脂質()5gを20mlのn−
ヘキサンに溶解して、20mlの5%含水エタノールを加
えて震とう後、ヘキサン層(上層)と含水エタノール層
(下層)をそれぞれ分け取り、上層には20mlの5%含
水エタノールを、下層には20mlのn−ヘキサンを加え
て再度震とうした。それぞれの上層を分け取り、2kPa
,60℃で溶媒留去し、4.5gの残渣を得た。10
0gのシリカゲルをn−ヘキサンで充填したカラムに、
前記残渣を5mlのn−ヘキサンで溶解した溶液をSV
1.0で通液した後に、n−ヘキサン:ジエチルエーテ
ル(20:1)500mlを通液してカラムから流出した
液の320〜480mlの画分を分取した。この画分を2
kPa ,60℃で溶媒留去し、0.31gの脂質を得た。
この脂質には、MK−7 15.4%が含有されてお
り、TLCで観察したところ上記の他にトリグリセライ
ド、ステロールおよびその誘導体、炭化水素類がみられ
た。MK−7の回収率は68%であった。Example 6 5 g of the lipid () obtained in Example 2 above was added to 20 ml of n-
After dissolving in hexane and adding 20 ml of 5% hydrous ethanol and shaking, separate the hexane layer (upper layer) and the hydrous ethanol layer (lower layer), respectively, and 20 ml of 5% hydrous ethanol for the upper layer and the lower layer for 20 ml of n-hexane was added and the mixture was shaken again. Separate each upper layer 2kPa
The solvent was distilled off at 60 ° C. to obtain 4.5 g of residue. 10
A column filled with 0 g of silica gel with n-hexane,
A solution prepared by dissolving the above residue with 5 ml of n-hexane was added to SV.
After passing through 1.0, 500 ml of n-hexane: diethyl ether (20: 1) was passed through, and 320 to 480 ml fractions of the liquid flowing out from the column were collected. 2 for this fraction
The solvent was distilled off at kPa and 60 ° C. to obtain 0.31 g of lipid.
This lipid contained 15.4% of MK-7, and when observed by TLC, triglyceride, sterol and its derivative, and hydrocarbons were found in addition to the above. The recovery rate of MK-7 was 68%.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 A61K 31/12 ADT 9455−4C C07C 46/10 C11B 1/10 3/10 3/12 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location A61K 31/12 ADT 9455-4C C07C 46/10 C11B 1/10 3/10 3/12
Claims (13)
た天然メナキノン−7高含量脂質。1. A natural menaquinone-7 high-content lipid extracted from a food material fermented with Bacillus subtilis.
項第1項記載の天然メナキノン−7高含量脂質。2. The natural menaquinone-7 high-content lipid according to claim 1, wherein the extracting method is extraction.
ン−7が分解しない条件下で精製することである請求項
第1項記載の天然メナキノン−7高含量脂質。3. The natural menaquinone-7-rich lipid according to claim 1, wherein the extracting method is extraction and purification under a condition that natural menaquinone-7 is not decomposed.
工過程で発生する粕、煮汁などの副産物である請求項第
1項ないし第3項のいずれか一項記載の天然メナキノン
−7高含量脂質。4. The natural menaquinone-7 high-content lipid according to any one of claims 1 to 3, wherein the food material is an edible plant or a by-product such as meal or broth produced in the process of processing them.
上、時間48時間以上であることを特徴とする請求項第
1項ないし第4項のいずれか一項記載の天然メナキノン
−7高含量脂質。5. The high content of natural menaquinone-7 according to any one of claims 1 to 4, wherein the fermentation condition with Bacillus subtilis is a temperature of 42 ° C. or higher and a time of 48 hours or longer. Lipids.
し第5項のいずれか一項記載の天然メナキノン−7高含
量脂質。6. The natural menaquinone-7-rich lipid according to any one of claims 1 to 5, wherein the Bacillus subtilis is Bacillus natto.
以上である請求項第1項ないし第6項のいずれか一項記
載の天然メナキノン−7高含量脂質。7. The content of natural menaquinone-7 is 200 ppm.
The natural menaquinone-7 high content lipid according to any one of claims 1 to 6, which is the above.
ない条件下における精製方法が、溶媒抽出、溶媒分別、
吸着分別、蒸留、クロマトグラフィーまたは膜分離の単
独もしくはそれらを2以上複合した方法である請求項第
3項ないし第7項のいずれか一項記載の天然メナキノン
−7高含量脂質。8. A method of extraction and purification under the condition that natural menaquinone-7 is not decomposed includes solvent extraction, solvent fractionation,
The natural menaquinone-7 high-content lipid according to any one of claims 3 to 7, which is a method of adsorption fractionation, distillation, chromatography or membrane separation alone or a combination of two or more thereof.
溶媒あるいは含水有機溶媒である請求項第2項ないし第
8項のいずれか一項記載の天然メナキノン−7高含量脂
質。9. The natural menaquinone-7 high-content lipid according to any one of claims 2 to 8, wherein the solvent used for extraction or purification is an organic solvent or a water-containing organic solvent.
溶離によって成される請求項第8項記載の天然メナキノ
ン−7高含量脂質。10. The adsorption fractionation method comprises adsorption on activated carbon,
The natural menaquinone-7-rich lipid according to claim 8, which is formed by elution.
の高真空蒸留である請求項第8項記載の天然メナキノン
−7高含量脂質。11. The natural menaquinone-7 high content lipid according to claim 8, wherein the distillation method is high vacuum distillation such as molecular distillation or steam distillation.
素あるいはアルコール、エーテル、エステル、ケトンで
ある請求項第9項記載の天然メナキノン−7高含量脂
質。12. The natural menaquinone-7 high content lipid according to claim 9, wherein the organic solvent is a hydrocarbon having 1 to 10 carbon atoms or alcohol, ether, ester or ketone.
か一項記載の天然メナキノン−7高含量脂質を主成分と
する、骨粗鬆症の予防または/かつ治療用組成物。13. A composition for preventing or / and treating osteoporosis, which comprises a natural menaquinone-7-rich lipid according to any one of claims 1 to 12 as a main component.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7196007A JP2900238B2 (en) | 1994-07-07 | 1995-07-07 | Natural Menaquinone-7 High Lipid Content |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17950494 | 1994-07-07 | ||
| JP6-179504 | 1994-07-07 | ||
| JP7196007A JP2900238B2 (en) | 1994-07-07 | 1995-07-07 | Natural Menaquinone-7 High Lipid Content |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0873396A true JPH0873396A (en) | 1996-03-19 |
| JP2900238B2 JP2900238B2 (en) | 1999-06-02 |
Family
ID=26499337
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7196007A Expired - Lifetime JP2900238B2 (en) | 1994-07-07 | 1995-07-07 | Natural Menaquinone-7 High Lipid Content |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2900238B2 (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1036256A (en) * | 1996-07-23 | 1998-02-10 | Masayoshi Yamaguchi | Anti-osteoporosis composition |
| WO2001036591A1 (en) * | 1999-11-16 | 2001-05-25 | Honda Trading Corporation | Yunnan sl-001 strain |
| US6677141B2 (en) | 1998-05-17 | 2004-01-13 | Honda Trading Corporation | Edible compositions of Bacillus subtilis natto cells containing water-soluble vitamin K |
| JP2006325597A (en) * | 2006-06-15 | 2006-12-07 | Nippon Seibutsu Kagaku Kenkyusho:Kk | How to recover vitamin K2 |
| WO2007148494A1 (en) | 2006-06-23 | 2007-12-27 | J-Oil Mills, Inc. | Agent for increasing testosterone level |
| WO2008126367A1 (en) | 2007-04-05 | 2008-10-23 | J-Oil Mills, Inc. | Ataractic agent and functional food |
| JP2012097039A (en) * | 2010-11-02 | 2012-05-24 | Kao Corp | Autoinducer-2 inhibitor, and preventing and/or therapeutic agent of periodontal disease or caries disease |
| JP5062922B2 (en) * | 2011-02-14 | 2012-10-31 | 株式会社J−オイルミルズ | Skin collagen production promoter |
| JP5066720B2 (en) * | 2005-04-27 | 2012-11-07 | 国立大学法人豊橋技術科学大学 | Quinone profile method using quinone compounds extracted using compressed carbon dioxide |
| WO2014017145A1 (en) | 2012-07-24 | 2014-01-30 | 株式会社J-オイルミルズ | Composition |
| WO2016027300A1 (en) * | 2014-08-19 | 2016-02-25 | 不二製油グループ本社株式会社 | Culture containing menaquinone-7, and method for producing menaquinone-7 |
| JP2022520180A (en) * | 2019-07-02 | 2022-03-29 | サンゲン バイオサイエンス カンパニー,リミテッド | Production method of natto bacteria and MK-7 |
| EP4001421A1 (en) | 2020-11-16 | 2022-05-25 | Endektovet Ltd | Method for obtaining oil extract of menaquinone-7 from fermentation broth |
| WO2023043218A1 (en) * | 2021-09-17 | 2023-03-23 | 주식회사 지에프퍼멘텍 | Composition comprising extract from cell mass of bacillus subtilis natto for improving memory |
-
1995
- 1995-07-07 JP JP7196007A patent/JP2900238B2/en not_active Expired - Lifetime
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1036256A (en) * | 1996-07-23 | 1998-02-10 | Masayoshi Yamaguchi | Anti-osteoporosis composition |
| US6677141B2 (en) | 1998-05-17 | 2004-01-13 | Honda Trading Corporation | Edible compositions of Bacillus subtilis natto cells containing water-soluble vitamin K |
| US6677143B2 (en) | 1998-05-17 | 2004-01-13 | Honda Trading Company | Method for culturing Bacillus subtilis natto to produce water-soluble vitamin K and food product, beverage, or feed containing the cultured microorganism or the vitamin K derivative |
| WO2001036591A1 (en) * | 1999-11-16 | 2001-05-25 | Honda Trading Corporation | Yunnan sl-001 strain |
| US6420145B1 (en) | 1999-11-16 | 2002-07-16 | Honda Trading Corporation | Yunnan SL-001 strain |
| JP5066720B2 (en) * | 2005-04-27 | 2012-11-07 | 国立大学法人豊橋技術科学大学 | Quinone profile method using quinone compounds extracted using compressed carbon dioxide |
| JP2006325597A (en) * | 2006-06-15 | 2006-12-07 | Nippon Seibutsu Kagaku Kenkyusho:Kk | How to recover vitamin K2 |
| WO2007148494A1 (en) | 2006-06-23 | 2007-12-27 | J-Oil Mills, Inc. | Agent for increasing testosterone level |
| WO2008126367A1 (en) | 2007-04-05 | 2008-10-23 | J-Oil Mills, Inc. | Ataractic agent and functional food |
| JP2012097039A (en) * | 2010-11-02 | 2012-05-24 | Kao Corp | Autoinducer-2 inhibitor, and preventing and/or therapeutic agent of periodontal disease or caries disease |
| JP5062922B2 (en) * | 2011-02-14 | 2012-10-31 | 株式会社J−オイルミルズ | Skin collagen production promoter |
| US9486398B2 (en) | 2012-07-24 | 2016-11-08 | J-Oil Mills, Inc. | Composition |
| WO2014017145A1 (en) | 2012-07-24 | 2014-01-30 | 株式会社J-オイルミルズ | Composition |
| US10039704B2 (en) | 2012-07-24 | 2018-08-07 | J-Oil Mills, Inc. | Composition |
| WO2016027300A1 (en) * | 2014-08-19 | 2016-02-25 | 不二製油グループ本社株式会社 | Culture containing menaquinone-7, and method for producing menaquinone-7 |
| JPWO2016027300A1 (en) * | 2014-08-19 | 2017-06-01 | 不二製油株式会社 | Menaquinone-7-containing culture and method for producing menaquinone-7 |
| JP2022520180A (en) * | 2019-07-02 | 2022-03-29 | サンゲン バイオサイエンス カンパニー,リミテッド | Production method of natto bacteria and MK-7 |
| US12460235B2 (en) | 2019-07-02 | 2025-11-04 | Sungen Bioscience Co., Ltd. | Bacillus subtilis natto and method for producing MK-7 |
| EP4001421A1 (en) | 2020-11-16 | 2022-05-25 | Endektovet Ltd | Method for obtaining oil extract of menaquinone-7 from fermentation broth |
| WO2023043218A1 (en) * | 2021-09-17 | 2023-03-23 | 주식회사 지에프퍼멘텍 | Composition comprising extract from cell mass of bacillus subtilis natto for improving memory |
| KR20230041337A (en) * | 2021-09-17 | 2023-03-24 | 주식회사 지에프퍼멘텍 | Compositon for Improving Memory Containing Culture Extract of Bacillus Subtilis Natto |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2900238B2 (en) | 1999-06-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4703060A (en) | Nutritive compositions containing fatty substances and a process for the preparation thereof | |
| US6740778B2 (en) | Method for the preparation of oleanolic acid and/or maslinic acid | |
| CN105287666B (en) | A kind of preparation method of Seabuckthorm Seed Oil | |
| CN112739440B (en) | Eutectic extract formation and purification | |
| US5985344A (en) | Process for obtaining micronutrient enriched rice bran oil | |
| US5847238A (en) | Processes for recovering xanthophylls from corn gluten meal | |
| US5612485A (en) | High cis beta-carotene composition | |
| JP2900238B2 (en) | Natural Menaquinone-7 High Lipid Content | |
| JPH02215351A (en) | Method for collecting krill phospholipid and functional food and nerve function improving agent having nerve function improving effect | |
| MXPA02003076A (en) | Method for extracting compounds of furan lipids and polyhydroxylated fatty alcohols of avocado, composition based on said compounds and use of said compounds in therapy, cosmetics and food. | |
| CN111117773B (en) | Method for separating nervonic acid from garlic oil and application thereof | |
| JP5463526B2 (en) | Dried defatted cereal meal with adsorbed and concentrated health functional ingredients, concentrate of health functional ingredients prepared from the meal, and methods for producing them | |
| Singanusong et al. | Micronutrients in rice bran oil | |
| KR20120139690A (en) | Liquid / liquid extraction | |
| JPH11193238A (en) | Barley malt oil containing plant ceramide-related substance and method for producing the same | |
| CN1651383A (en) | Preparation method of natural crystalline gingerol | |
| CN1293963A (en) | Health-care microalga food and its preparing process | |
| JP5637707B2 (en) | Skillpsin B-containing composition and method for producing skillpsin B-containing composition | |
| JP2943031B2 (en) | Method for producing natural vitamin K concentrate | |
| JP2001097983A (en) | Plant extract containing sphingolipid and method for producing the same | |
| JP2000044468A (en) | Lipase inhibitor and antiobestic medicine or hyperlipidemia inhibitor | |
| JP2003119492A (en) | Method for purifying sphingolipids | |
| AU2006313172A1 (en) | Method of refining episesamin | |
| JP6951736B2 (en) | Cerebroside manufacturing method and cerebroside purification kit | |
| CN120209927A (en) | A method for preparing high-DHA, high-phospholipid, odorless krill oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090319 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100319 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100319 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100319 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110319 Year of fee payment: 12 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110319 Year of fee payment: 12 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120319 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120319 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130319 Year of fee payment: 14 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130319 Year of fee payment: 14 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140319 Year of fee payment: 15 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| EXPY | Cancellation because of completion of term |