JPH06113871A - Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits - Google Patents

Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits

Info

Publication number
JPH06113871A
JPH06113871A JP4264829A JP26482992A JPH06113871A JP H06113871 A JPH06113871 A JP H06113871A JP 4264829 A JP4264829 A JP 4264829A JP 26482992 A JP26482992 A JP 26482992A JP H06113871 A JPH06113871 A JP H06113871A
Authority
JP
Japan
Prior art keywords
limonoid
flavonoid
compound
citrus fruits
recovering
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4264829A
Other languages
Japanese (ja)
Inventor
Hisao Maeda
久夫 前田
Masaki Miyake
正起 三宅
Shinya Inaba
伸也 稲葉
Shigeru Ayano
茂 綾野
Yoshihiko Ozaki
嘉彦 尾崎
Kiyoshi Ifuku
清 伊福
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.)
WAKAYAMA AGURI BIO KENKYU CENT
WAKAYAMA AGURI BIO KENKYU CENTER KK
Original Assignee
WAKAYAMA AGURI BIO KENKYU CENT
WAKAYAMA AGURI BIO KENKYU CENTER 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 WAKAYAMA AGURI BIO KENKYU CENT, WAKAYAMA AGURI BIO KENKYU CENTER KK filed Critical WAKAYAMA AGURI BIO KENKYU CENT
Priority to JP4264829A priority Critical patent/JPH06113871A/en
Publication of JPH06113871A publication Critical patent/JPH06113871A/en
Pending legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

PURPOSE:To obtain a method for separating and recovering a flavonoid and a limonoid compounds in which the flavonoid and limonoid compounds contained in citrus fruits can be separated and economically and advantageously recovered. CONSTITUTION:The objective method for separating and recovering a flavonoid and a limonoid compounds comprises the first step of adding a microorganism or a yeast to a marc of citrus fruits and subjecting impurities to the decomposing treatment and the second step of centrifuging the resultant treated substance obtained in the first step into a precipitated fraction containing the flavonoid compound and a supernatant fraction containing the limonoid compound.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は柑橘類に含有されている
健胃、鎮咳、去炎さらに血圧降下作用などの薬理活性を
有するフラボノイド化合物と抗ガン活性、昆虫に対する
摂食阻害活性などの生理活性を有するリモノイド化合物
とを効率的に分離回収する方法に関するものである。
FIELD OF THE INVENTION The present invention relates to flavonoid compounds contained in citrus fruits having pharmacological activities such as stomach, antitussive, anti-inflammatory and hypotensive action, and anti-cancer activity, and physiological activity such as antifeedant activity against insects. The present invention relates to a method for efficiently separating and recovering a limonoid compound having

【0002】[0002]

【従来の技術】ミカン、夏ミカン、八朔、グレープフル
ーツなどの柑橘類果実は、搾汁しジュースにして飲料と
して供されることが多いが、果汁加工工場などで多量に
搾汁する場合、搾汁粕も多量に発生する。加工工場など
で多量に発生した搾汁粕は、そのまま廃棄すると環境汚
染などを引き起こす虞があるため、通常、加熱乾燥する
などして家畜の飼料などに使用されている。
2. Description of the Related Art Citrus fruits such as mandarin orange, summer mandarin orange, Hachisaku, and grapefruit are often squeezed into juice and used as beverages. Also occurs in large quantities. The squeezed lees that are produced in large quantities in processing factories may cause environmental pollution if they are discarded as they are. Therefore, they are usually used for livestock feed by heating and drying.

【0003】[0003]

【発明が解決しようとする課題】しかし、搾汁粕中に
は、健胃、鎮咳、去炎さらに血圧降下作用などの薬理活
性を有するフラボノイド化合物と抗ガン活性、昆虫に対
する摂食阻害活性などの生理活性を有するリモノイド化
合物が含有されており、これらの有効利用を図る研究が
行われている。
However, in the squeezed lees, flavonoid compounds having pharmacological activities such as stomach, antitussive, anti-inflammatory and hypotensive action, anti-cancer activity, antifeedant activity against insects, etc. A limonoid compound having physiological activity is contained, and studies are being conducted to make effective use thereof.

【0004】因に、柑橘搾汁粕からフラボノイド化合物
を抽出、回収する技術については、生搾汁粕および乾燥
搾汁粕(乾燥果皮)からアルカリ抽出することによるヘ
スペリジンの採取が知られているが、柑橘搾汁粕中には
夾雑物が多く含有されているため、ヘスペリジンの抽出
効果が悪く工業的な実用化には到っていない。また、リ
モノイド化合物はこれまで柑橘果汁の苦味成分としてと
らえられ、脱苦味という観点で研究が進められてきた
が、工業的な抽出、回収については全く報告されていな
い。
[0004] Incidentally, as a technique for extracting and recovering flavonoid compounds from citrus juice residue, it is known to collect hesperidin by extracting alkali from raw juice residue and dried juice residue (dry skin). Since many impurities are contained in the citrus juice cake, the extraction effect of hesperidin is poor and it has not been put to industrial use. Further, limonoid compounds have been regarded as bitterness components of citrus fruit juice, and research has been advanced from the viewpoint of debittering, but no industrial extraction or recovery has been reported.

【0005】本発明は、このような事情に鑑みて、柑橘
類に含まれるフラボノイド化合物およびリモノイド化合
物を分離して経済的に有利に回収することができる分離
回収方法を提供することを目的としている。
In view of such circumstances, it is an object of the present invention to provide a separation and recovery method capable of separating flavonoid compounds and limonoid compounds contained in citrus fruits and recovering them economically advantageously.

【0006】[0006]

【課題を解決するための手段】本発明にかかる柑橘類に
含有されるフラボノイド化合物およびリモノイド化合物
の分離回収方法は、このような目的を達成するために、
柑橘類果実の搾汁粕に微生物あるいは酵素を加えて夾雑
物を分解処理する第1工程、第1工程で得た処理物を、
フラボノイド化合物を含む沈澱画分とリモノイド化合物
を含む上澄み画分とに遠心分離する第2工程を実施する
ようにした。
The method for separating and recovering flavonoid compounds and limonoid compounds contained in citrus fruits according to the present invention, in order to achieve such an object,
The first step of adding microorganisms or enzymes to the citrus fruit juice cake to decompose contaminants, and the treated product obtained in the first step,
A second step of centrifuging into a precipitate fraction containing flavonoid compounds and a supernatant fraction containing limonoid compounds was performed.

【0007】上記構成において、搾汁粕とは、一次搾汁
粕(生搾汁粕)だけでなく、二次搾汁粕(生搾汁粕に石
灰を加え圧搾し脱水処理した搾汁粕)も含まれる。ま
た、第1工程において、微生物あるいは酵素を加える前
に、搾汁粕に等量以上の水を加えるとともに、pHを酵
素および微生物に合わせて調整したり、搾汁粕を80℃
以上に加熱し、予め搾汁粕の加熱殺菌を行うことが好ま
しい。
In the above construction, the squeezed lees are not only primary squeezed lees (raw squeezed lees) but also secondary squeezed lees (squeezed lees obtained by pressing and dehydrating raw squeezed lees with lime). Is also included. In addition, in the first step, before adding the microorganisms or enzymes, an equal amount or more of water is added to the squeezed lees, and the pH is adjusted according to the enzymes and the microorganisms,
It is preferable that the squeezed lees are heated and sterilized by heating as above.

【0008】第1工程で使用する酵素としては、ペクチ
ナーゼ、セルラーゼ、アミラーゼ、プロテアーセ、リパ
ーゼ等が挙げられるが、Aspergillus ni
gerAspergillus oryzaeAs
pergillus pulverulentusなど
のアスペルギルス属(糸状菌の一種)を起源とするペク
チナーゼや、Aspergillus nigerなど
のアスペルギルス属またはTrichoderma
irideなどトリコデルマ属(糸状菌の一種)を起源
とするセルラーゼが特に好ましい。
Examples of the enzyme used in the first step include pectinase, cellulase, amylase, protease and lipase. Aspergillus ni
ger , Aspergillus oryzae , As
pectinases originating from the genus Aspergillus (a type of filamentous fungus) such as pergillus pulverulentus, and genus Aspergillus such as Aspergillus niger or Trichoderma v
Cellulase originating from the genus Trichoderma (a type of filamentous fungus) such as iride is particularly preferable.

【0009】第1工程における酵素による夾雑物の分解
処理温度は、40〜50℃程度が好ましく、酵素添加量
は、原料搾汁粕に対して0.02〜0.2重量%程度が
好ましい。反応時間は酵素添加量により異なり、たとえ
ば、0.02%では2日間、0.2%では16時間以内
で十分である。
The temperature for decomposing contaminants by the enzyme in the first step is preferably about 40 to 50 ° C., and the amount of enzyme added is preferably about 0.02 to 0.2% by weight with respect to the raw material squeezed lees. The reaction time varies depending on the amount of enzyme added. For example, 0.02% is 2 days, and 0.2% is 16 hours or less.

【0010】また第1工程において酵素剤を用いる代わ
りに上記酵素を産出する微生物を用いる事ができる。第
1工程で使用する微生物としては、Aspergill
us nigerAspergillus oryz
aeAspergillus pulverulen
tusなどのアスペルギルス属(糸状菌の一種)やTr
ichoderma virideなどトリコデルマ属
(糸状菌の一種)等が挙げられる。
Further, instead of using the enzyme agent in the first step, a microorganism producing the above enzyme can be used. As the microorganism used in the first step, Aspergill
us niger , Aspergillus oryz
ae , Aspergillus pulverulen
genus Aspergillus (a type of filamentous fungus) such as tus or Tr
The genus Trichoderma (a type of filamentous fungus) such as ichoderma viride can be mentioned.

【0011】そして、微生物はあらかじめ麦芽汁、麹
汁、ポテトデキストロース液などの液体培養基中で培養
しておき、菌液の形で搾汁粕に加えることが好ましい。
微生物による夾雑物の分解処理温度は、30〜40℃程
度とし、3〜5日間培養(静置培養または振盪培養;振
盪培養の方が培養時間は短時間で良い)処理することが
好ましい。
It is preferable that the microorganism is previously cultivated in a liquid culture medium such as wort, koji or potato dextrose solution, and then added to the squeezed lees in the form of a bacterial solution.
The temperature for decomposing contaminants by microorganisms is preferably about 30 to 40 ° C., and the treatment is preferably performed for 3 to 5 days (static culture or shaking culture; shaking culture requires a shorter culture time).

【0012】また、第1工程において微生物を使用した
場合は、一定期間培養後培養液中の菌体を除去した後、
遠心分離処理を行うことが好ましい。なお、フラボノイ
ド化合物の回収率をより高めるためには第2工程におい
て得た沈澱画分に等量またはそれ以上の水を加え、攪拌
した後、さらに遠心分離(水洗)したり、第1工程終了
後、第2工程の遠心分離を行う前に、篩分によって15
0μm以下の画分のみを回収する(150μmを越える
画分は除去する)ようにすることが好ましい。
When a microorganism is used in the first step, after culturing for a certain period of time and removing the cells in the culture solution,
It is preferable to perform centrifugation. In order to increase the recovery rate of the flavonoid compound, an equal amount or more of water is added to the precipitate fraction obtained in the second step, the mixture is stirred, and then centrifuged (washed), or the first step is completed. After that, before performing the centrifugation in the second step, the
It is preferable to collect only the fraction of 0 μm or less (remove the fraction of more than 150 μm).

【0013】また、第2工程で得た上澄み画分に含まれ
るリモノイド化合物は、合成吸着樹脂あるいは陰イオン
交換樹脂に吸着せしめ、糖類などの夾雑物を除去した
後、メチルアルコールなど非水系溶媒で溶出し、減圧濃
縮法により容易に高濃度化が可能となる。この場合、酵
素処理を行うことにより、上澄液量が増加し、抽出され
るリモノイド化合物の絶対量が増加すると共に、水溶性
の多糖類が低分子化することにより、リモノイド化合物
の純度が高められるという利点を有する。
The limonoid compound contained in the supernatant fraction obtained in the second step is adsorbed on a synthetic adsorption resin or an anion exchange resin to remove impurities such as sugars, and then a non-aqueous solvent such as methyl alcohol. After elution, the concentration can be easily increased by the vacuum concentration method. In this case, by performing the enzyme treatment, the amount of the supernatant increases, the absolute amount of the extracted limonoid compound increases, and the water-soluble polysaccharide has a low molecular weight, thereby increasing the purity of the limonoid compound. Has the advantage that

【0014】[0014]

【作用】上記構成によれば、第1工程において、酵素お
よび微生物を搾汁粕に添加することによって搾汁粕中の
夾雑物(ペクチンやセルロース等)を分解して糖などの
水溶性物質にしたのち、第2工程で遠心分離すると、沈
澱画分と上澄み画分とに分離される。
According to the above construction, in the first step, the enzymes and the microorganisms are added to the squeezed meal to decompose the contaminants (pectin, cellulose, etc.) in the squeezed meal to form water-soluble substances such as sugars. After that, when it is centrifuged in the second step, it is separated into a precipitate fraction and a supernatant fraction.

【0015】こうして得た沈澱画分には、フラボノイド
化合物が多量に含まれ、上澄み画分には、糖などととも
にリモノイド化合物が多量に含まれている。
The precipitate fraction thus obtained contains a large amount of flavonoid compounds, and the supernatant fraction contains a large amount of limonoid compounds as well as sugars.

【0016】[0016]

【実施例】以下に、本発明を、その実施例を参照しつつ
詳しく説明する。
EXAMPLES The present invention will be described in detail below with reference to its examples.

【0017】[0017]

【実施例1】柑橘果実の搾汁粕中の有用物質の一つであ
るフラボノイド化合物を効率的に抽出、回収するため、
含有している夾雑物を分解除去するのに有効な酵素の選
択を行った。温州ミカンの二次搾汁粕に等量の水を加
え、希塩酸でpH4.0に調整し、加熱殺菌(85℃)
後、冷却(50℃)し、市販酸素剤を0.1重量%割合
となるように加えた。このとき用いた酸素剤は48種で
あり、その主たる活性からペクチナーゼ、セルラーゼ、
アミラーゼ、プロテアーゼ、リパーゼに分類し、各々p
H4.0,pH4.0,pH5.0,pH7.0,pH
7.0に調整し50℃で24時間静置し酵素反応を行わ
せた。続いて遠心分離(10000rpm,10分間)
を行い、沈澱画分を得た。
Example 1 In order to efficiently extract and recover a flavonoid compound, which is one of useful substances in citrus fruit juice cake,
An enzyme effective for decomposing and removing the contained impurities was selected. Equivalent amount of water is added to the secondary squeezed lees of Satsuma mandarin, pH is adjusted to 4.0 with dilute hydrochloric acid, and heat sterilization (85 ° C)
After that, the mixture was cooled (50 ° C.), and a commercial oxygen agent was added so that the ratio was 0.1% by weight. There were 48 kinds of oxygen agents used at this time, and pectinase, cellulase,
It is classified into amylase, protease, and lipase, and each is
H4.0, pH4.0, pH5.0, pH7.0, pH
It was adjusted to 7.0 and left to stand at 50 ° C. for 24 hours for enzyme reaction. Subsequently, centrifugation (10,000 rpm, 10 minutes)
The precipitation fraction was obtained.

【0018】この沈澱画分を乾燥後、固形物歩留り、フ
ラボノイド化合物の1つであるヘスペリジン濃度および
ヘスペリジン歩留りを求め、表1に示した。
After the precipitation fraction was dried, the solids retention, the concentration of hesperidin, which is one of the flavonoid compounds, and the hesperidin retention were determined and are shown in Table 1.

【0019】[0019]

【表1】 [Table 1]

【0020】表1に示すように、酵素剤としてペクチナ
ーゼやセルラーゼを用いた場合、夾雑物の除去率が高く
得られた固形物の歩留りが小さく、ヘスペリジン濃度の
高いことが示された。特にペクチナーゼを主としセルラ
ーゼ、ヘミセルラーゼ活性を有する酵素剤についてはそ
の効果が大きかった。またいずれの酵素によってもヘス
ペリジンの損失は特に認められなかった。
As shown in Table 1, it was shown that when pectinase or cellulase was used as the enzyme agent, the removal rate of contaminants was high, the yield of the obtained solids was small, and the concentration of hesperidin was high. In particular, the effect was large for the enzyme agents mainly containing pectinase and having cellulase and hemicellulase activities. Moreover, no loss of hesperidin was observed by any of the enzymes.

【0021】[0021]

【実施例2】主としてペクチナーゼ活性を有する酵素お
よびセルラーゼ活性を有する酵素を等量混合し、実施例
1と同様に酵素処理を行った。つまり温州ミカン二次搾
汁粕に等量の水を加え、希塩酸でpH4.0に調整し、
加熱殺菌(85℃)後、冷却(50℃)し、混合酵素剤
を0.1重量%の割合となるように加えた。
Example 2 Mainly, an enzyme having pectinase activity and an enzyme having cellulase activity were mixed in equal amounts, and the same enzyme treatment as in Example 1 was performed. In other words, add an equal amount of water to Satsuma mandarin secondary juice and adjust the pH to 4.0 with dilute hydrochloric acid.
After heat sterilization (85 ° C.), the mixture was cooled (50 ° C.), and the mixed enzyme preparation was added at a ratio of 0.1% by weight.

【0022】そして、50℃、24時間酵素反応をさせ
た後、500μm以上、300−500μm、150−
300μm、150μm以下の各画分に篩分し、それぞ
れ遠心分離により沈澱物を得、さらに沈澱物を5倍量の
水で水洗し、遠心分離により沈澱画分を回収した。得ら
れた沈澱画分の固形物歩留り、ヘスペリジン濃度、ヘス
ペリジン歩留りを測定し、表2に示した。
After enzymatic reaction at 50 ° C. for 24 hours, 500 μm or more, 300-500 μm, 150-
The fractions of 300 μm and 150 μm or less were sieved, and a precipitate was obtained by centrifugation, and the precipitate was washed with 5 times the amount of water, and the precipitate fraction was recovered by centrifugation. The solid yield, hesperidin concentration, and hesperidin yield of the obtained precipitation fraction were measured and are shown in Table 2.

【0023】[0023]

【表2】 [Table 2]

【0024】表2に示すように、混合酵素を用いること
により、夾雑物の除去率が高まり、固形物歩留りが大幅
に減少することによって、ヘスペリジン濃度の増加が認
められた。特に150μm以下の画分のヘスペリジン濃
度が27.4%となり、未処理(ヘスペリジン濃度6.
4%)の約4.3倍に高められた。
As shown in Table 2, by using the mixed enzyme, the removal rate of contaminants was increased and the solids yield was significantly reduced, whereby the concentration of hesperidin was increased. Especially, the hesperidin concentration of the fraction of 150 μm or less was 27.4%, and the untreated (hesperidin concentration 6.
4%) to about 4.3 times.

【0025】[0025]

【実施例3】搾汁粕を含む培地中でペクチナーゼやセル
ラーゼ活性を有すると思われる糸状菌(Aspergi
llus aculeatusAspergillu
sawamoriAspergillus fumi
gatusAspergillus niger
spergillus usamii)を培養し、夾雑
物の分解を行った。すなわち、まず温州ミカン搾汁粕
(二次搾汁粕)に1.5倍量の水を加え、pH4.0に
調整し、加熱殺菌(85℃)した後、30〜40℃に冷
却した時点で、あらかじめポテトテキストロース液で培
養しておいた菌液(搾汁粕の0.5倍量)を加えた。そ
して、30℃で3日間培養(静置培養)した後培養液中
の菌体を除去し、遠心分離処理(10000rpm,1
0分間)により沈澱画分を得た。得られた沈澱画分の固
形物歩留り、ヘスペリジン濃度、ヘスペリジン歩留りを
測定し、表3に示した。
Example 3 Filamentous fungi suspected of having pectinase and cellulase activities in a medium containing squeezed lees ( Aspergi
llus aculeatus, Aspergillu
sawamori , Aspergillus fumi
gasus , Aspergillus niger , A
spergillus usamii ) was cultured to decompose contaminants. That is, first, 1.5 times the amount of water was added to the Satsuma mandarin orange cake (secondary cake) to adjust the pH to 4.0, heat sterilize (85 ° C), and then cool to 30-40 ° C. Then, a bacterial solution (0.5 times the amount of squeezed lees) that had been previously cultured in a potato sucrose solution was added. Then, after culturing at 3O <0> C for 3 days (stationary culturing), the bacterial cells in the culture broth were removed, followed by centrifugation (10000 rpm, 1
A precipitation fraction was obtained by (0 minutes). The solid yield, hesperidin concentration, and hesperidin yield of the obtained precipitation fraction were measured and shown in Table 3.

【0026】[0026]

【表3】 [Table 3]

【0027】表3に示すよう、各菌体の培養液について
酵素活性を測定した結果、いずれもペクチナーゼ、セル
ラーゼ及びヘミセルラーゼ活性が認められ、固形物残存
率についても減少した。また微生物培養中のヘスペリジ
ンの損失も特に認められず、結果としてヘスペリジン濃
度の高い画分を得ることが可能であった。
As shown in Table 3, as a result of measuring the enzyme activity of the culture solution of each microbial cell, pectinase, cellulase and hemicellulase activities were observed in all cases, and the solid content residual rate was also reduced. In addition, no loss of hesperidin was observed during the microorganism culture, and as a result, it was possible to obtain a fraction having a high hesperidin concentration.

【0028】[0028]

【実施例4】温州ミカン搾汁粕からリノモイド配糖体を
回収する目的で、搾汁粕(1000g)に等量の水を加
え、希塩酸でpH4.0に調整し、加熱殺菌(85℃)
後、冷却(50℃) し、ペクチナーゼ活性、セルラーゼ
活性、ヘミセルラーゼ活性を有する市販酵素剤(上田化
学工業(株)製 セルロシンPE100)を0.1重量%の割
合となるように加え、50℃で24時間静置し酵素反応
を行わせた。酵素処理後遠心分離(10000rpm,
10分間)し、上澄み画分(上澄み液)1600gを得
た。得られた上澄み画分を合成吸着樹脂(オルガノ
(株)製 Amberlite XAD-2)150mlに吸着せしめ、水
(150ml) で糖類などの夾雑物を除去したのち、メチ
ルアルコール(450ml) で溶出させることで、リモノ
イド配糖体を含む画分を得た。
[Example 4] For the purpose of recovering linomoid glycosides from Satsuma mandarin orange juice, an equal amount of water was added to the juice cake (1000 g), pH was adjusted to 4.0 with dilute hydrochloric acid, and heat sterilization was performed (85 ° C).
Then, the mixture was cooled (50 ° C), and a commercially available enzyme preparation having pectinase activity, cellulase activity, and hemicellulase activity (Cellulosin PE100 manufactured by Ueda Chemical Industry Co., Ltd.) was added at a ratio of 0.1% by weight, and the mixture was added at 50 ° C. The mixture was allowed to stand for 24 hours to carry out an enzymatic reaction. Centrifugation after enzyme treatment (10,000 rpm,
After 10 minutes, 1600 g of a supernatant fraction (supernatant solution) was obtained. Adsorb the obtained supernatant fraction to 150 ml of synthetic adsorption resin (Amberlite XAD-2 manufactured by Organo Corporation), remove impurities such as sugars with water (150 ml), and elute with methyl alcohol (450 ml). Then, a fraction containing a limonoid glycoside was obtained.

【0029】搾汁粕,酵素処理液(上澄み画分)、メタ
ノール溶出液のそれぞれについてリモノイド配糖体の含
有濃度を調べ、その結果を表4に示した。
The concentration of limonoid glycosides in each of the squeezed lees, the enzyme-treated solution (supernatant fraction) and the methanol eluate was examined, and the results are shown in Table 4.

【0030】[0030]

【表4】 [Table 4]

【0031】なお、メタノール溶出液から減圧濃縮法で
メチルアルコールを除去することによって成分組成に影
響することなく容易にリモノイド配糖体の濃度をさらに
高濃度化することができた。
By removing methyl alcohol from the methanol eluate by a vacuum concentration method, the concentration of limonoid glycosides could be easily increased without affecting the component composition.

【0032】[0032]

【発明の効果】本発明にかかる柑橘類に含有されるフラ
ボノイド化合物およびリモノイド化合物の分離回収方法
は、以上のように構成されており、柑橘類に含まれるフ
ラボノイド化合物またはリモノイド化合物をそれぞれ高
濃度に含む画分に分離することができる。
The method for separating and recovering flavonoid compounds and limonoid compounds contained in citrus fruits according to the present invention is constituted as described above, and the flavonoid compounds or limonoid compounds contained in citrus fruits are contained in high concentrations. Can be separated into minutes.

【0033】そして、このフラボノイド化合物またはリ
モノイド化合物を高濃度で含む画分を濃縮などすること
で、フラボノイド化合物またはリモノイド化合物を経済
的に有利に回収することができる。
The flavonoid compound or limonoid compound can be economically and advantageously recovered by concentrating the fraction containing the flavonoid compound or limonoid compound at a high concentration.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 尾崎 嘉彦 和歌山県海草郡下津町坪1501−2 (72)発明者 伊福 清 和歌山市西浜3−7−84 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Yoshihiko Ozaki 1501-2 Tsubo, Shimotsu-cho, Seagrass-gun, Wakayama Prefecture (72) Inventor Kiyoshi Ifuku 3-7-84 Nishihama, Wakayama-shi

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】柑橘類果実の搾汁粕に微生物あるいは酵素
を加えて夾雑物を分解処理する第1工程、第1工程で得
た処理物を、フラボノイド化合物を含む沈澱画分とリモ
ノイド化合物を含む上澄み画分とに遠心分離する第2工
程を備えている柑橘類中のフラボノイド化合物およびリ
モノイド化合物の分離回収方法。
1. A first step in which microorganisms or enzymes are added to squeezed lees of citrus fruits to decompose impurities, and the treated product obtained in the first step contains a precipitation fraction containing a flavonoid compound and a limonoid compound. A method for separating and collecting flavonoid compounds and limonoid compounds in citrus fruits, which comprises a second step of centrifuging with a supernatant fraction.
JP4264829A 1992-10-02 1992-10-02 Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits Pending JPH06113871A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4264829A JPH06113871A (en) 1992-10-02 1992-10-02 Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4264829A JPH06113871A (en) 1992-10-02 1992-10-02 Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits

Publications (1)

Publication Number Publication Date
JPH06113871A true JPH06113871A (en) 1994-04-26

Family

ID=17408791

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4264829A Pending JPH06113871A (en) 1992-10-02 1992-10-02 Method for separating and recovering flavonoid compound and limonoid compound contained in citrus fruits

Country Status (1)

Country Link
JP (1) JPH06113871A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5734046A (en) * 1995-10-17 1998-03-31 The United States Of America As Represented By The Secretary Of Agriculture Method for manufacturing limonoid glucosides
US6409996B1 (en) * 1997-11-19 2002-06-25 Flavone Sunproducts A/S Composition comprising one or more flavonoids, method of obtaining such composition and use thereof as UV-absorbing agent
JP2007223914A (en) * 2006-02-21 2007-09-06 Unitika Ltd Oral administration formulation
JP2008206479A (en) * 2007-02-27 2008-09-11 Hiroshi Takahashi Phytochemical extracting method and phytochemical extract obtained by this method
JP2013021949A (en) * 2011-07-19 2013-02-04 Tokushima Prefecture Sprouted brown rice containing citrus sudachi polyphenol
JP2013021950A (en) * 2011-07-19 2013-02-04 Tokushima Prefecture Method for manufacturing citrus sudachi polyphenol from sudachi (squeezed juice residue)
JP2020174679A (en) * 2020-08-04 2020-10-29 サントリーホールディングス株式会社 Pericarp extract and method for producing the same

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5734046A (en) * 1995-10-17 1998-03-31 The United States Of America As Represented By The Secretary Of Agriculture Method for manufacturing limonoid glucosides
US6409996B1 (en) * 1997-11-19 2002-06-25 Flavone Sunproducts A/S Composition comprising one or more flavonoids, method of obtaining such composition and use thereof as UV-absorbing agent
JP2007223914A (en) * 2006-02-21 2007-09-06 Unitika Ltd Oral administration formulation
JP2008206479A (en) * 2007-02-27 2008-09-11 Hiroshi Takahashi Phytochemical extracting method and phytochemical extract obtained by this method
JP2013021949A (en) * 2011-07-19 2013-02-04 Tokushima Prefecture Sprouted brown rice containing citrus sudachi polyphenol
JP2013021950A (en) * 2011-07-19 2013-02-04 Tokushima Prefecture Method for manufacturing citrus sudachi polyphenol from sudachi (squeezed juice residue)
JP2020174679A (en) * 2020-08-04 2020-10-29 サントリーホールディングス株式会社 Pericarp extract and method for producing the same

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