JP2000072790A - Method of removing residual agrochemical in plant extract - Google Patents

Method of removing residual agrochemical in plant extract

Info

Publication number
JP2000072790A
JP2000072790A JP26102898A JP26102898A JP2000072790A JP 2000072790 A JP2000072790 A JP 2000072790A JP 26102898 A JP26102898 A JP 26102898A JP 26102898 A JP26102898 A JP 26102898A JP 2000072790 A JP2000072790 A JP 2000072790A
Authority
JP
Japan
Prior art keywords
solution
adsorption resin
plant extract
treatment
solvent
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
JP26102898A
Other languages
Japanese (ja)
Inventor
Yoshitaka Nakamura
喜孝 中村
浩誠 ▲桑▼原
Hiromoto Kuwabara
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.)
Maruzen Pharmaceutical Co Ltd
Original Assignee
Maruzen Pharmaceutical 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 Maruzen Pharmaceutical Co Ltd filed Critical Maruzen Pharmaceutical Co Ltd
Priority to JP26102898A priority Critical patent/JP2000072790A/en
Publication of JP2000072790A publication Critical patent/JP2000072790A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method that can readily remove residual agrochemicals from plant extracts to be used as food, cosmetic, medicine and the like, when residual agrochemicals of organic chlorine compounds having strong toxicity, for example, BHC or DDT, are detected in the extracts. SOLUTION: A plant extract including residual agrochemicals of organic chlorine compounds is dissolved in a mixture of a lower aliphatic alcohol and water at a volume ratio of 10/90-80/20. Then, the resultant solution is brought into contact with a porous adsorption resin having pores with a modal radius of 30-120 Å thereby adsorbing the residual agrochemicals in the solution into the adsorption resin.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、食品、化粧料、医
薬品等の構成成分として利用しようとする植物抽出物が
人体に有害な有機塩素化合物系の残留農薬を含有する場
合にそれを除去する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is to remove a plant extract to be used as a component of foods, cosmetics, pharmaceuticals, etc., when an organic chlorine compound-based pesticide residue harmful to the human body is contained. It is about the method.

【0002】[0002]

【従来の技術】近年、食品添加物、化粧料構成成分、医
薬品、医薬部外品等、様々な分野で化学合成品よりも安
全性の点で優れている天然物を利用しようとする傾向が
強まり、それにともない植物体が含有する有用成分の研
究が進んだ結果、様々な植物体からの抽出物が多くの用
途に提供されるようになった。
2. Description of the Related Art In recent years, there has been a tendency to use natural products that are superior in safety to chemically synthesized products in various fields, such as food additives, cosmetic components, pharmaceuticals, quasi-drugs, and the like. As a result, research on useful components contained in plants has progressed, and as a result, extracts from various plants have been provided for many uses.

【0003】しかしながら、本質的には安全な筈の植物
抽出物にも有害な残留農薬が検出されることがあり、そ
の対策が問題になっている。
However, harmful pesticides may be detected in plant extracts which should be essentially safe, and countermeasures have become a problem.

【0004】植物抽出物から残留農薬が検出される原因
は二つあって、一つは原料植物の栽培過程で使用された
農薬が付着もしくは吸収されていた場合であり一つは過
去に使用された農薬のうち分解せずに土壌中に蓄積され
ていたものを原料植物が根から吸収した場合である。し
たがって、安全性に問題があることがわかって現在は使
われていない有機塩素化合物系農薬、たとえばBHCや
DDTでも、中国、インド、東南アジア、アフリカ等で
は使用禁止になるのが遅かったこともあって、いまだに
植物抽出物から検出される例が後を絶たない。薬効が優
れていたため広範囲に且つ長期間使用され、一時期代表
的な殺虫剤であったBHCとDDTは、自然界において
分解しにくいため長年月にわたりそのままの形で土壌中
に残り、それが植物に吸収されたり自然界の食物連鎖に
取り込まれて拡散したりしているのである。
There are two reasons why pesticide residues are detected from plant extracts. One is that pesticides used in the cultivation process of raw material plants are attached or absorbed, and the other is that pesticides used in the past have been used. This is the case where the source plant absorbed the pesticides accumulated in the soil without decomposition from the roots. Therefore, the use of organochlorine pesticides, such as BHC and DDT, which have been found to be problematic for safety and are not currently used, has been delayed from being banned in China, India, Southeast Asia and Africa. Nevertheless, there are still many cases detected in plant extracts. BHC and DDT, which have been widely used for a long time due to their excellent medicinal properties, and have been used for a long period of time, and are difficult to decompose in nature, remain in the soil for many months as they are, and are absorbed by plants. It is being spread or taken in the natural food chain.

【0005】したがって、栽培植物はもちろん、農薬が
使われたことがない筈の山野に自生する植物にも農薬が
含まれていることがあり、植物抽出物を利用する場合は
必ず残留農薬の有無を検査し、もし農薬が検出された場
合は可能な限りそれを除去した上で使用に供することが
必要になる。
[0005] Therefore, pesticides may be contained not only in cultivated plants but also in plants that grow naturally in mountainous areas where pesticides have never been used. It is necessary to inspect pesticides, and if pesticides are detected, remove them as much as possible before using them.

【0006】[0006]

【発明が解決しようとする課題】そこで本発明の目的
は、なんらかの用途に利用しようとする植物抽出物に残
留農薬が検出された場合にその残留農薬を除去する方法
を提供することにあり、特に、残留農薬の中でも出現頻
度が高く毒性も強い有機塩素化合物系のもの、たとえば
BHCやDDTの除去に有効な方法を提供することにあ
る。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a method for removing pesticide residues when the pesticide residues are detected in a plant extract to be used for any purpose. It is another object of the present invention to provide an effective method for removing organochlorine compounds of high frequency and high toxicity among pesticide residues, for example, BHC and DDT.

【0007】[0007]

【課題を解決するための手段】本発明による残留農薬除
去法は、特定範囲の含水率の含水低級脂肪族アルコール
に溶けた状態の植物抽出物中の有機塩素化合物系残留農
薬が特定の細孔径を有する多孔性吸着樹脂に選択的に吸
着されることを見いだしたことに基づくものであって、
有機塩素化合物系の残留農薬を含有する植物抽出物を体
積比で10:90ないし80:20の低級脂肪族アルコ
ールと水との混合液に溶解させ、得られた溶液を細孔の
最頻度半径が30〜120Åである多孔性吸着樹脂に接
触させて溶液中の残留農薬を該吸着樹脂に吸着させ、処
理後の溶液より植物抽出物を回収することを特徴とす
る。
According to the present invention, there is provided a method for removing pesticide residues, the method comprising removing an organochlorine compound-based pesticide from a plant extract dissolved in a water-containing lower aliphatic alcohol having a specific range of water content to a specific pore size. Based on the finding that it is selectively adsorbed on a porous adsorption resin having
A plant extract containing an organic chlorine compound-based pesticide residue is dissolved in a mixture of lower aliphatic alcohol and water in a volume ratio of 10:90 to 80:20, and the resulting solution is subjected to the most frequent radius of pores. Is contacted with a porous adsorption resin having a temperature of 30 to 120 ° to adsorb residual pesticides in the solution to the adsorption resin, and a plant extract is recovered from the solution after the treatment.

【0008】[0008]

【発明の実施の形態】本発明の残留農薬除去法において
は、処理対象となる植物抽出物をまず体積比で10:9
0ないし80:20の低級脂肪族アルコールと水との混
合液(以下、処理液溶媒という)に適当濃度に溶解させ
る。このとき用いる低級脂肪族アルコールとしては、メ
タノール、エタノール、イソプロパノール等が適当であ
るが、安全性も考慮すると、エタノールが最も好まし
い。なお、植物抽出物の種類によっては上記処理液溶媒
を用いて澄明な溶液とすることが難しく一部が溶解せず
に分散状態になる場合があるが、そのような場合でも、
残留農薬の大部分は上記含水アルコールに溶解するので
処理は可能である。
BEST MODE FOR CARRYING OUT THE INVENTION In the method for removing pesticide residues according to the present invention, a plant extract to be treated is first treated with a volume ratio of 10: 9.
It is dissolved at a suitable concentration in a mixture of a lower aliphatic alcohol of 0 to 80:20 and water (hereinafter referred to as a treatment liquid solvent). As the lower aliphatic alcohol used at this time, methanol, ethanol, isopropanol and the like are suitable, but ethanol is most preferable in consideration of safety. Depending on the type of plant extract, it may be difficult to obtain a clear solution using the treatment liquid solvent described above, and a part may be in a dispersed state without being dissolved, but in such a case,
Most of the residual pesticides can be treated because they are dissolved in the above-mentioned aqueous alcohol.

【0009】処理液溶媒のアルコールと水の比率は上記
範囲内にあることが重要であって、アルコールの比率が
10vol%未満であると残留農薬だけでなく植物抽出物
中の有用成分まで吸着されて、処理による損失が増え
る。反対にアルコールの比率が80vol%をこえると、
残留農薬が吸着樹脂に吸着されにくくなり、約90vol
%以上ではほとんど吸着されなくなる。
It is important that the ratio of alcohol to water in the solvent of the treatment liquid is within the above range. If the alcohol ratio is less than 10 vol%, not only residual pesticides but also useful components in plant extracts are adsorbed. As a result, processing losses increase. Conversely, if the alcohol ratio exceeds 80 vol%,
Residual agricultural chemicals are less likely to be adsorbed by the adsorption resin, about 90vol
%, It is hardly adsorbed.

【0010】吸着樹脂に接触させる植物抽出物溶液は固
形または液状の植物抽出物を上記処理液溶媒に溶かして
調製したものに限られるわけではなく、抽出溶媒が処理
液溶媒と同一組成のものであるならば、原料植物から得
られたままの抽出液の状態のものでもよい。また、濃
縮、溶媒添加等により抽出液の溶媒組成を調整して処理
液溶媒と同じ組成にしたものも、同様に被処理溶液とす
ることができる。
The plant extract solution to be brought into contact with the adsorption resin is not limited to a solution prepared by dissolving a solid or liquid plant extract in the above-mentioned solvent for the treatment liquid. If there is, it may be in the state of an extract as obtained from the raw material plant. A solution to be treated may be similarly prepared by adjusting the solvent composition of the extract to the same composition as the solvent of the treatment liquid by concentration, addition of a solvent, or the like.

【0011】処理に用いる多孔性吸着樹脂は、スチレン
とジビニルベンゼンの三次元的共重合体またはそのベン
ゼン環の一部の水素原子を臭素で置換して疎水性を高め
たものからなる、イオン交換基を有しないものである。
また、その細孔群の最頻度半径が30〜120Åのもの
である。これよりも細孔径が小さいものは、吸着樹脂内
細孔へ残留農薬が拡散しにくく、残留農薬の除去率が悪
くなる。一方、細孔径がこれよりも大きいと、有用成分
の吸着損失は少ないが残留農薬を吸着して除去する能力
も低くなる。
The porous adsorbent resin used in the treatment is a three-dimensional copolymer of styrene and divinylbenzene or one obtained by replacing a part of hydrogen atoms of the benzene ring with bromine to increase the hydrophobicity. It has no group.
The most frequent radius of the group of pores is 30 to 120 °. If the pore size is smaller than this, the residual pesticide hardly diffuses into the pores in the adsorption resin, and the removal rate of the residual pesticide becomes poor. On the other hand, if the pore diameter is larger than this, the loss of adsorption of useful components is small, but the ability to adsorb and remove residual pesticides is also low.

【0012】使用可能な吸着樹脂の具体例としては、ダ
イヤイオンHP21、同30、同40、同50、セパビ
ーズSP207、同825、同850(以上、いずれも
三菱化学株式会社製品)、アンバーライトXAD2、同
4、同7(以上、いずれもオルガノ株式会社製品)等が
ある。
Specific examples of usable adsorption resins include Diaion HP21, 30, 30, 40, 50, Sepabeads SP207, 825, and 850 (all of which are products of Mitsubishi Chemical Corporation) and Amberlite XAD2. , And 4 and 7 (both are products of Organo Corporation).

【0013】用意された処理溶液を吸着樹脂と接触させ
る方法は、特に限定されるものではない。吸着樹脂を充
填したカラムに処理溶液を上または下から流すのが最も
適当であるが、回分式の処理槽に処理溶液と吸着樹脂を
入れて撹拌してもよい。カラム処理を行う場合、通液速
度はSVとして0.3〜3.0/hが適当である。処理に
用いる吸着樹脂は、あらかじめ処理液溶媒と同一組成の
溶媒と接触させ、該溶媒で細孔を満たしておくことが望
ましい。
The method for bringing the prepared treatment solution into contact with the adsorption resin is not particularly limited. It is most appropriate to flow the processing solution from above or below the column filled with the adsorption resin, but it is also possible to put the processing solution and the adsorption resin in a batch type processing tank and stir. In the case of performing column treatment, it is appropriate that the liquid passing speed is 0.3 to 3.0 / h as SV. It is desirable that the adsorption resin used in the treatment is brought into contact with a solvent having the same composition as the solvent of the treatment liquid in advance and the pores are filled with the solvent.

【0014】処理溶液中の残留農薬は、上記吸着樹脂と
接触したとき吸着樹脂の細孔中に入り込んで吸着され
る。一方、植物抽出物中の有用成分、たとえばポリフェ
ノール、サポニン、ビタミン類、色素、テルペノイド等
は、処理液溶媒に対する溶解性が大である一方で疎水性
の吸着樹脂に対する親和性はあまり無いので、細孔中に
吸着されず、溶液中に止まる。したがって、処理後の溶
液を濃縮、乾燥するなどして採取される抽出物は、処理
前の抽出物に含まれていた残留農薬のほとんどが除去さ
れたものとなる。
When the pesticide residue in the treatment solution comes into contact with the adsorption resin, it enters the pores of the adsorption resin and is adsorbed. On the other hand, useful components in plant extracts, such as polyphenols, saponins, vitamins, pigments, terpenoids, etc., have high solubility in the treatment liquid solvent but do not have much affinity for the hydrophobic adsorption resin. It is not adsorbed in pores and stays in solution. Therefore, the extract obtained by concentrating and drying the solution after the treatment is one from which most of the residual pesticide contained in the extract before the treatment has been removed.

【0015】処理に用いた吸着樹脂は、90%以上の低
級脂肪族アルコールによる通液洗浄等により再生して再
利用することができる。
The adsorbing resin used in the treatment can be regenerated and reused by washing with 90% or more of lower aliphatic alcohol by passing it through.

【0016】本発明の方法は、最も普通に検出される残
留農薬であるBHC、DDT(類似の殺虫剤であるDD
D,DDE等を含む)、その他アルドリン、ディルドリ
ン、エンドリン、ヘプタクロル、ヘプタクロルエポキシ
ド等の有機塩素化合物系農薬の除去に有効である。
The method of the present invention relates to the most commonly detected pesticide residues, BHC, DDT (a similar insecticide, DD).
D, DDE, etc.), and other organic chlorine compound pesticides such as aldrin, dieldrin, endrin, heptachlor, heptachlor epoxide, and the like.

【0017】本発明の残留農薬除去方法は、処理液溶媒
にまったく溶解せず分散させることも不可能な植物抽出
物には原理的に適用困難であるが、医薬、化粧料、食品
等の分野で利用される植物抽出物にそのようなものはほ
とんど無いから、事実上すべての植物抽出物に適用可能
である。すなわち、アザミ、アマチャ、アヘン、アロエ
ベア、イチョウ、ウイキョウ、ウコン、ウスベニアオ
イ、ウラジロガシ、エイジツ、エゾウコギ、延命草、黄
精、オウギ、オウゴン、オウバク、大麦、オトギリ草、
柿、カミツレ、甘草、キダチアロエ、ギムネマ、キャベ
ツ、玉竹、キラヤ、金銀花、菊花、クコ、紅参、苦参、
熊笹、クワ、月桂樹葉、決明子、ゲンチアナ、小麦、
米、ゴボウ、ゴマ、サルビア、サンザ、紫蘇、サンシ
シ、サンシュ、山椒、山薬、椎茸、紫恨、芍薬、車前
草、十薬、生姜、白樺、スギナ、ステビア、センキュ
ウ、センナ、センブリ、ソバ、大根、タイソウ、大豆、
タマリンド、タラ、チンピ、当帰、トチュウ、冬虫夏
草、トウモロコシ、刺梨、人参、忍冬、パセリ、浜防
風、ハマメリス、姫松茸、ビルベリー、ビワ、ブクリョ
ウ、ブドウ、ブルーベリー、ヘチマ、ヘマティン、菩提
樹、牡丹皮、ホップ、松葉、桃、メリッサ、ユッカ、ヨ
クイニン、ヨモギ、ライ麦、ラカンカ、緑茶、リンゴ、
ルイボス、ルスカス、霊芝、連銭草、ローズヒップ、ロ
ーズマリー等からの様々な溶媒による抽出物を対象とし
て実施可能である。
The method for removing pesticide residues according to the present invention is in principle difficult to apply to plant extracts which are completely insoluble and cannot be dispersed in the solvent of the processing solution, but are indispensable in the fields of medicine, cosmetics, foods and the like. Since there is very little such in the plant extracts utilized in the above, it is applicable to virtually all plant extracts. That is, thistle, amateur, opium, aloe-bear, ginkgo, fennel, turmeric, usbnia oyster, vladinki, edibles, elephant grass, prolonged life grass, yellow sperm, maggot, giant gourd, maggot, barley, genus grass,
Persimmon, chamomile, licorice, kidachi aloe, gymnema, cabbage, tamatake, kiraya, gold and silver flower, chrysanthemum flower, wolfberry, red ginseng, bittersweet,
Kumasa, mulberry, bay leaves, Akiko, gentian, wheat,
Rice, Burdock, Sesame, Salvia, Sanza, Shiso, Sanshishi, Sanshu, Sansho, Sanpaku, Shiitake, Shiitake, Shakuyaku, Carabusa, Jujube, Ginger, Birch, Japanese horsetail, Stevia, Senkyu, Senna, Senburi, Japanese radish , Daisies, soybeans,
Tamarind, cod, cock, toki, eucommia, caterpillar, corn, stinging pear, carrot, shin winter, parsley, beach windbreak, hamamelis, himematsutake, bilberry, loquat, boukuro, grape, blueberry, loofah, hematin, bodhi tree, peony, Hops, pine needles, peaches, melissa, yucca, yoquinin, mugwort, rye, lakanka, green tea, apple,
The method can be applied to extracts with various solvents from rooibos, ruscath, reishi, reenzo, rosehip, rosemary and the like.

【0018】[0018]

【実施例】実施例1,比較例1,2 中国産の紅参3kgを濃度30vol%の含水エタノールで
1時間還流抽出し、抽出残渣について再度同様の抽出処
理を行い、得られた合計48リットルの抽出液を減圧下
に濃縮して濃縮液3kgを得た。
EXAMPLES Example 1 and Comparative Examples 1 and 2 3 kg of Chinese red ginseng was extracted with 30 vol% aqueous ethanol under reflux for 1 hour, and the extraction residue was subjected to the same extraction treatment again to obtain a total of 48 liters. The extract was concentrated under reduced pressure to obtain 3 kg of a concentrate.

【0019】この濃縮液は、1kg当たり固形分を362
g、粗サポニンを106g含有し、さらにBHC0.6
0mg、DDT0.40mgを含有するものであった。
This concentrated liquid has a solid content of 362 per kg.
g, 106 g of crude saponin, and BHC 0.6
It contained 0 mg and 0.40 mg of DDT.

【0020】上記抽出液濃縮液を1kgずつに3分し、そ
れらにエタノールと水を加えて、溶媒中のエタノール濃
度の異なる3種類の吸着樹脂処理液(固形分濃度5.5
重量%)を調製し、各処理液について下記の吸着樹脂処
理を行なった。
The above extract concentrate is divided into 3 parts each for 1 kg, and ethanol and water are added thereto, and three kinds of adsorbing resin treatment liquids having different ethanol concentrations in the solvent (solid concentration 5.5).
% By weight), and the treatment liquid was subjected to the following adsorption resin treatment.

【0021】吸着樹脂処理条件:多孔性吸着樹脂・ダイ
ヤイオンHP−21(最頻度細孔径80Å)1リットル
を内径10cmのカラムに充填し、処理液溶媒と同じ組成
の溶媒でカラム内を満たしておく。このカラムに吸着樹
脂処理液をSV=0.3/hで通液し、その後、処理液溶
媒と同じ組成の溶媒3リットルでカラムを洗浄する。
Adsorption resin treatment conditions: 1 liter of a porous adsorption resin, Diaion HP-21 (most frequently 80 μm in diameter) was packed in a column having an inner diameter of 10 cm, and the inside of the column was filled with a solvent having the same composition as the solvent of the processing liquid. deep. The adsorption resin treatment liquid is passed through this column at SV = 0.3 / h, and then the column is washed with 3 liters of a solvent having the same composition as the treatment liquid solvent.

【0022】上記吸着樹脂処理でカラムを通過した処理
液と洗浄液とを合わせ、全量が約2kgになるまで濃縮
し、得られた濃縮液について、固形分、粗サポニン、B
HCおよびDDTを定量した。その結果を表1に示す。
The processing solution passed through the column in the above-mentioned adsorption resin treatment and the washing solution are combined and concentrated until the total amount becomes about 2 kg. The obtained concentrated solution contains solid content, crude saponin, B
HC and DDT were quantified. Table 1 shows the results.

【0023】[0023]

【表1】 比較例1 実施例1 比較例2 処理液溶媒エタノール濃度 5vol% 50vol% 90vol% 固形分回収率(%) 79.0 89.8 98.1 粗サポニン回収率(%) 49.1 99.1 99.1 BHC除去率(%) 100 100 11.7 DDT除去率(%) 100 100 22.5Table 1 Comparative Example 1 Example 1 Comparative Example 2 Solvent Ethanol Concentration of Treatment Solution 5 vol% 50 vol% 90 vol% Solids Recovery (%) 79.0 89.8 98.1 Crude Saponin Recovery (%) 49.1 99.1 99.1 BHC removal rate (%) 100 100 11.7 DDT removal rate (%) 100 100 22.5

【0024】実施例2,比較例3,4 中国産の緑茶葉3kgを濃度50vol%の含水エタノール
で1時間還流抽出し、抽出残渣について再度同様の抽出
処理を行い、得られた合計37リットルの抽出液を減圧
下に濃縮して濃縮液3kgを得た。
Example 2 and Comparative Examples 3 and 3 3 kg of Chinese green tea leaves were refluxed and extracted with 50% by volume of aqueous ethanol for 1 hour, and the extraction residue was subjected to the same extraction treatment again to obtain a total of 37 liters. The extract was concentrated under reduced pressure to obtain 3 kg of a concentrate.

【0025】この濃縮液は、1kg当たり固形分を354
g、ポリフェノールを148g含有し、さらにBHC
0.36mg、DDT0.20mgを含有するものであった。
This concentrated liquid has a solid content of 354 per kg.
g, 148 g of polyphenol, and BHC
It contained 0.36 mg and 0.20 mg of DDT.

【0026】上記抽出液濃縮液を1kgずつに3分し、そ
れらにエタノールと水を加えて、溶媒中のエタノール濃
度の異なる3種類の吸着樹脂処理液(固形分濃度5.5
重量%)を調製し、各処理液について下記の吸着樹脂処
理を行なった。
The above extract concentrate is divided into 3 parts each of 1 kg, and ethanol and water are added thereto, and the three kinds of adsorbent resin treatment liquids having different ethanol concentrations in the solvent (solids concentration of 5.5) are added.
% By weight), and the treatment liquid was subjected to the following adsorption resin treatment.

【0027】吸着樹脂処理条件:多孔性吸着樹脂・セパ
ビーズSP−825(最頻度細孔径57Å)1リットル
を内径10cmのカラムに充填し、処理液溶媒と同じ組成
の溶媒でカラム内を満たしておく。このカラムに吸着樹
脂処理液をSV=0.5/hで通液し、その後、処理液溶
媒と同じ組成の溶媒3リットルでカラムを洗浄する。
Adsorption resin treatment conditions: 1 liter of porous adsorption resin, Sepabead SP-825 (most frequent pore diameter 57 °) is packed in a column having an inner diameter of 10 cm, and the inside of the column is filled with a solvent having the same composition as the solvent of the processing liquid. . The adsorption resin treatment liquid is passed through this column at SV = 0.5 / h, and then the column is washed with 3 liters of a solvent having the same composition as the treatment liquid solvent.

【0028】上記吸着樹脂処理でカラムを通過した処理
液と洗浄液とを合わせ、全量が約2kgになるまで濃縮
し、得られた濃縮液について、固形分、ポリフェノー
ル、BHCおよびDDTを定量した。その結果を表2に
示す。
The treatment liquid passed through the column in the adsorption resin treatment and the washing liquid were combined, concentrated until the total amount became about 2 kg, and the solid content, polyphenol, BHC and DDT of the obtained concentrated liquid were quantified. Table 2 shows the results.

【0029】[0029]

【表2】 比較例3 実施例2 比較例4 処理液溶媒エタノール濃度 5vol% 70vol% 90vol% 固形分回収率(%) 80.8 94.9 98.3 ポリフェノール回収率(%) 69.6 98.6 99.3 BHC除去率(%) 100 100 16.7 DDT除去率(%) 100 100 0Table 2 Comparative Example 3 Example 2 Comparative Example 4 Treatment Solution Solvent Ethanol Concentration 5 vol% 70 vol% 90 vol% Solids Recovery (%) 80.8 94.9 98.3 Polyphenol Recovery (%) 69.6 98 .6 99.3 BHC removal rate (%) 100 100 16.7 DDT removal rate (%) 100 100 0

【0030】比較例5〜7 吸着樹脂を最頻度細孔径が260ÅのダイヤイオンHP
−20に変更したほかは実施例1と同様にした吸着樹脂
処理の結果は表3のとおりであった。
Comparative Examples 5 to 7 Adsorption resin was used as Diaion HP having a most frequent pore diameter of 260 °.
Table 3 shows the results of the adsorption resin treatment performed in the same manner as in Example 1 except that the value was changed to -20.

【0031】[0031]

【表3】 比較例5 比較例6 比較例7 処理液溶媒エタノール濃度 5vol% 50vol% 90vol% 固形分回収率(%) 77.9 91.7 97.8 粗サポニン回収率(%) 76.4 97.2 99.1 BHC除去率(%) 91.7 56.7 0.02 DDT除去率(%) 95.0 62.5 0.08Table 3 Comparative Example 5 Comparative Example 6 Comparative Example 7 Treatment Solution Solvent Ethanol Concentration 5 vol% 50 vol% 90 vol% Solids Recovery (%) 77.9 91.7 97.8 Crude Saponin Recovery (%) 76.4 97.2 99.1 BHC removal rate (%) 91.7 56.7 0.02 DDT removal rate (%) 95.0 62.5 0.08

【0032】[0032]

【発明の効果】上述のように、本発明によれば植物抽出
物中の有機塩素化合物系残留農薬を簡単な操作でほぼ完
全に除去することができ、有用成分の損失も僅少で済
む。
As described above, according to the present invention, organic chlorine compound-based pesticide residues in a plant extract can be almost completely removed by a simple operation, and the loss of useful components can be minimized.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4C057 AA10 AA30 BB02 DD01 JJ52 4H006 AA02 AD16 AD17 BB14 4H055 AA02 AB10 AB12 AB20 AD32 BA01 BA30 CA60  ──────────────────────────────────────────────────続 き Continued on front page F term (reference) 4C057 AA10 AA30 BB02 DD01 JJ52 4H006 AA02 AD16 AD17 BB14 4H055 AA02 AB10 AB12 AB20 AD32 BA01 BA30 CA60

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 有機塩素化合物系の残留農薬を含有する
植物抽出物を体積比で10:90ないし80:20の低
級脂肪族アルコールと水との混合液に溶解させ、得られ
た溶液を細孔の最頻度半径が30〜120Åである多孔
性吸着樹脂に接触させて溶液中の残留農薬を該吸着樹脂
に吸着させ、処理後の溶液より植物抽出物を回収するこ
とを特徴とする植物抽出物中の残留農薬を除去する方
法。
1. A plant extract containing an organic chlorine compound-based pesticide residue is dissolved in a mixed solution of lower aliphatic alcohol and water in a volume ratio of 10:90 to 80:20, and the resulting solution is finely divided. A plant extraction method comprising contacting a porous adsorbent resin having pores with a most frequent radius of 30 to 120 ° to adsorb residual pesticides in the solution to the adsorbent resin, and recovering a plant extract from the treated solution. A method for removing pesticide residues in goods.
【請求項2】 低級脂肪族アルコールとしてエタノール
を用いる請求項1記載の方法。
2. The method according to claim 1, wherein ethanol is used as the lower aliphatic alcohol.
【請求項3】 残留農薬がBHCまたは(および)DD
Tである請求項1記載の方法。
3. The method according to claim 1, wherein the pesticide residue is BHC or (and) DD.
The method of claim 1, wherein T is T.
JP26102898A 1998-09-01 1998-09-01 Method of removing residual agrochemical in plant extract Pending JP2000072790A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JP2000072790A true JP2000072790A (en) 2000-03-07

Family

ID=17356055

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Country Link
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002080946A1 (en) * 2001-04-02 2002-10-17 Wakamoto Pharmaceutical Co.,Ltd. Compositions for preventing and/or treating oral diseases
KR100377539B1 (en) * 2000-04-06 2003-03-26 광주과학기술원 Method for Detection of Toxicity of Pesticide Residues in Foods Using Bioluminescent Bacteria
JP2004275023A (en) * 2003-03-13 2004-10-07 Si Seiko Co Ltd System for removing pesticide residue
JP2006089414A (en) * 2004-09-24 2006-04-06 Japan Research & Development Association For New Functional Foods Method for removing residual agricultural chemical of plant extract and plant extract
JP2007143413A (en) * 2005-11-24 2007-06-14 Maruzen Pharmaceut Co Ltd Method for eliminating unfavorable smell-causing component and bitter taste component, method for producing quillai extract, and quillai extract
JP2009511643A (en) * 2005-06-21 2009-03-19 ザ・コカ−コーラ・カンパニー Method for removing contaminants from essential oils
CN102091438A (en) * 2010-12-29 2011-06-15 浙江绍兴东灵保健食品有限公司 Method for removing pesticide residue in plant extract
WO2011092840A1 (en) 2010-01-29 2011-08-04 小川香料株式会社 Method for manufacturing polymethoxyflavones that are highly stable over time and have reduced residual pesticide levels
US9580668B2 (en) 2008-11-11 2017-02-28 Takasago International Corporation Process for producing purified essential oil
KR102376179B1 (en) * 2021-11-29 2022-03-18 (주)건보 Method for producing ginseng concentrate with reduced pesticide and phthalate

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100377539B1 (en) * 2000-04-06 2003-03-26 광주과학기술원 Method for Detection of Toxicity of Pesticide Residues in Foods Using Bioluminescent Bacteria
WO2002080946A1 (en) * 2001-04-02 2002-10-17 Wakamoto Pharmaceutical Co.,Ltd. Compositions for preventing and/or treating oral diseases
JP2004275023A (en) * 2003-03-13 2004-10-07 Si Seiko Co Ltd System for removing pesticide residue
JP2006089414A (en) * 2004-09-24 2006-04-06 Japan Research & Development Association For New Functional Foods Method for removing residual agricultural chemical of plant extract and plant extract
JP2009511643A (en) * 2005-06-21 2009-03-19 ザ・コカ−コーラ・カンパニー Method for removing contaminants from essential oils
JP2007143413A (en) * 2005-11-24 2007-06-14 Maruzen Pharmaceut Co Ltd Method for eliminating unfavorable smell-causing component and bitter taste component, method for producing quillai extract, and quillai extract
US9580668B2 (en) 2008-11-11 2017-02-28 Takasago International Corporation Process for producing purified essential oil
WO2011092840A1 (en) 2010-01-29 2011-08-04 小川香料株式会社 Method for manufacturing polymethoxyflavones that are highly stable over time and have reduced residual pesticide levels
US8945646B2 (en) 2010-01-29 2015-02-03 Ogawa & Co., Ltd. Method for manufacturing polymethoxyflavones that are highly stable over time and have reduced residual pesticide levels
CN102091438A (en) * 2010-12-29 2011-06-15 浙江绍兴东灵保健食品有限公司 Method for removing pesticide residue in plant extract
KR102376179B1 (en) * 2021-11-29 2022-03-18 (주)건보 Method for producing ginseng concentrate with reduced pesticide and phthalate

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