JPH0362099B2 - - Google Patents
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- Publication number
- JPH0362099B2 JPH0362099B2 JP62265889A JP26588987A JPH0362099B2 JP H0362099 B2 JPH0362099 B2 JP H0362099B2 JP 62265889 A JP62265889 A JP 62265889A JP 26588987 A JP26588987 A JP 26588987A JP H0362099 B2 JPH0362099 B2 JP H0362099B2
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- JP
- Japan
- Prior art keywords
- deodorizing
- distilled
- solvent
- temperature
- mother liquor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Description
[産業上の利用分野]
本発明は、茶、椿、山茶花、月桂樹などの常緑
広葉樹等の植物から採取された植物成分を含有す
る不揮発性残渣物の少ない消臭、脱臭材に関する
ものである。
[従来技術及び発明が解決しようとする問題点]
従来、これら常緑広葉樹等の植物から採取され
た植物成分を含有する消臭、脱臭材としては、例
えば特公昭58−18098号公報に示す如きものが知
られている。そしてこのものは、これら広葉樹素
材を溶媒抽出または減圧蒸留の手段により得られ
た留出成分を、そのまま使用するか、あるいは留
出成分中の溶媒を留去しただけのものを使用して
いた。
しかるに溶媒抽出または減圧蒸留したままのも
ののなかには、常温で高沸点のもの、あるいは長
時間溶媒中で処理されたために生じた重合生成物
等の不純物がいまだ存在しており、これが消臭、
脱臭材中に存在してそのまま不揮発性の残渣物と
なつてしまう許りでなく、それ自体異臭を放つも
のがあり、またその状態では異臭を放たないが、
消臭、脱臭材を加熱処理して大気中に積極的に蒸
散させるようにして使用するような場合に、不揮
発性残渣の熱による変性作用が促進されて異臭が
発生することがあるうえに、不揮発性残渣によつ
て消臭、脱臭材の蒸散性能が著しく阻害されるな
どの欠点がある。そこで前記抽出物をさらに二次
処理して不揮発性残渣物を僅少にすることが提唱
されるが、今日に至るまで、強制的に蒸散気化さ
せたときに不揮発性残渣物を使用に殆ど問題を残
さないよう僅少にすることについて検討したもの
がないという実状にあつた。
[問題を解決するための手段]
本発明は、上記の如き実情に鑑みこれらの欠点
を一掃することができる植物成分を含有する不揮
発性残渣物の少ない消臭、脱臭材を提供すること
を目的として創案されたものであつて、常緑広葉
樹等の植物の葉を素材としてこれを溶媒抽出で一
次処理したものを母液とし、この一次処理した母
液をさらに大気圧下にて130℃以下の範囲の温度
で留出させて、その留出成分が加熱処理されて強
制的に蒸散気化せしめたときの不揮発性残渣物が
僅少になるようにした二次処理成分を有効成分と
していることを特徴とするものである。
そして本発明は、この構成によつて、常緑広葉
樹等の植物から採取した植物成分を含有する消
臭、脱臭材でありながら、そのもののなかに異臭
を放つ元になる不揮発性残渣物を可及的に含まな
い様にしたものである。
そして本発明に用いられる植物としては、茶、
椿、寒椿、山茶花、楠木、月桂樹、榊等の通常よ
く知られた植物の葉を素材とし、これらを単独若
しくは併用して用いることができるが、さらにこ
れらの葉は、生物であつてもあるいは半乾燥物、
乾燥物であつても良いものである。さらにこれら
の素材から消臭、脱臭材を抽出する溶媒として
は、メチルアルコール、エチルアルコール、n−
プロピルアルコール、イソプロピルアルコール、
n−ブチルアルコール、ジエチレングリコール、
プロピレングリコール等の低級アルコール系溶
媒、アセトン、メチルエチルケトン等のケトン系
溶媒、ジエチルエーテル、ジオキサン、テトラヒ
ドロフラン等のエーテル系溶媒が単独若しくは複
数の混合溶媒として、さらには水との混合溶媒と
して用いることができる。
そしてこれら常緑広葉樹等の植物の素材を溶媒
中にて還流し、あるいは溶媒中にて加熱撹拌する
ことで溶媒抽出をし、これを濾過あるいは減圧蒸
留することで抽出処理して原料残渣が分離され、
これによつて一次処理された母液が得られること
になる。そしてこの母液をさらに大気圧下におい
て蒸留をして二次処理することになる。
そして本発明は、略130℃以下(好ましくは120
℃以下)までの温度を蒸留上限温度として留出す
る蒸留成分を有効成分として含有するものである
が、この場合、溶媒の沸点が目標とする蒸留上限
温度以下のものである場合には、消臭、脱臭材
は、一緒に留出する溶媒をそのまま含んだものを
消臭、脱臭材の有効成分とすることができるが、
さらに溶媒が除去されたものを消臭、脱臭材の有
効成分とすることもできる。このとき、溶媒の除
去には、溶媒の沸点が蒸留上限温度以下のもので
ある場合に、その沸点が蒸留上限温度から可成り
低いものであるものでは、母液を蒸留する際に、
低沸点溶媒を留去した後、その溶媒沸点を越えた
温度から蒸留上限温度までの温度で留出する蒸留
成分を消臭、脱臭材の有効成分として採取するこ
とができるが、溶媒沸点が蒸留上限温度に近いも
のである場合には、溶媒とともに留出したものを
減圧蒸留等の手段によつて溶媒と消臭、脱臭材の
有効成分とを分離することができる。また沸点が
蒸留上限温度以上の溶媒である場合には、母液を
そのまま大気圧下にて蒸留し、蒸留上限温度以下
の温度で留出した蒸留成分がそのまま殆ど溶媒を
含まない消臭、脱臭材の有効成分となる。
この様にして得られた消臭、脱臭材の有効成分
は、単独若しくは他の消臭、脱臭材と混合して用
いることができることは勿論であるが、その使用
の形態としては、例えばエチルアルコール等の適
宜溶媒に希釈した液材やエアロゾルとして散布す
る等の一般的な使用形態で用いることもできる
が、さらに本発明の消臭、脱臭材を有効成分とし
て含む液材を、多孔質材料、毛細管集合体、ガラ
スマツト等を用いて形成される吸い上げ媒体が突
出するように設けられたタンク中に充填してお
き、そして吸い上げ媒体を加熱せしめることによ
つて、吸い上げ媒体を介して吸い上げられた消
臭、脱臭材を大気中に強制的に蒸散気化させるよ
うに構成された消臭、脱臭器に用いることもでき
る。
[効果]
本発明は、叙述の如く構成されるものであるか
ら、常緑広葉樹等の植物の葉から得られた植物成
分を含有する不揮発性残渣物の少ない消臭、脱臭
材の有効成分としては、初めに溶媒抽出によつて
一次処理されたものを、さらに大気圧下にて130
℃以下の温度で留出させるという二次処理して得
られたものを有効成分とするものであるから、気
化しやすいものが主成分と成つていて、蒸留残渣
のない極めて揮発し易い物質によつて組成される
ことになる。そして、二次処理する際の蒸留温度
が130℃を越えないようにすることによつて、そ
れよりも高温で揮発するフラボン系物質、不飽和
アルデヒド、不飽和カルボン酸、あるいはベンズ
アルデヒドのような芳香族系化合物等の経時変化
しやすく、そして異臭を放つ元になる高不揮発性
物質が極めて僅少であつて成分中に殆ど含まれて
おらず、従つてこのものを加熱処理することによ
つて大気中に強制的に蒸散気化させて使用しよう
とした場合に、従来のもののように、タンク中に
不揮発性残渣が多量に残つたり、加熱部に不揮発
性物質が溜つて目詰まりを起したりして液材の吸
い上げ性が早期のうちに低下し、しかも加熱によ
り不揮発性物質の変性が促進され反つて異臭が放
たれてしまうようなことがなく、長期に亘つて優
れた消臭、脱臭性能を維持できることになる。
以下、本発明を実施例によつてさらに具体的に
説明する。
実施例 1
常緑広葉樹等の植物の葉として茶樹の乾燥した
葉の粉末を用い、これの150gとエタノール500ml
とをソツクスレー抽出器に仕込み、24時間加熱還
流する。そして抽出液より原料残渣を濾過して除
去して545gの一次処理の母液を得る。次いでこ
の母液を、リービツヒコンデンサが組付けられた
枝付きの丸底フラスコに入れ、加熱蒸留する。そ
して温度130℃までのものを留出せしめることで、
二次処理されたエタノール溶液としての消臭、脱
臭材を430g得た。
実施例 2、3
前記実施例1と同様の手法に基づいて表−1に
示す如く植物を用いて一次処理の母液を抽出し、
この母液をさらに蒸留して二次処理して本発明の
消臭、脱臭材を得た。
実施例 4、5
前記実施例1と同様の手法に基づいて母液を
得、この母液をさらに蒸留処理したが、この場
合、まず溶媒をその沸点温度までの留出成分とし
て留去した後、溶媒沸点を越えた温度以上から
120℃または130℃までの温度で留出する有効成分
を採取した。その結果を表1に示す。
比較例 1
母液の生成は前記実施例2と同様の処方に従う
が、母液の二次処理による分留温度を150℃まで
として蒸留成分を490g採取した。
[Industrial Application Field] The present invention relates to deodorizing and deodorizing materials containing plant components collected from plants such as tea, camellia, sasanqua, and evergreen broad-leaved trees such as laurel, and which have little nonvolatile residue. [Prior Art and Problems to be Solved by the Invention] Conventionally, as deodorizing and deodorizing materials containing plant components collected from plants such as evergreen broad-leaved trees, there are, for example, those shown in Japanese Patent Publication No. 18098/1983. It has been known. In this method, the distillate components obtained from these hardwood materials by means of solvent extraction or vacuum distillation are used as they are, or those obtained by simply distilling off the solvent in the distillate components are used. However, impurities such as those with high boiling points at room temperature or polymerization products generated due to long-term treatment in solvents still exist in the products that have been extracted with solvent or distilled under reduced pressure.
It is not acceptable for them to exist in deodorizing materials and turn into non-volatile residues, and there are some that emit a strange odor by themselves, and even though they do not emit a strange odor in that state,
When deodorizing and deodorizing materials are heat-treated and used to actively evaporate into the atmosphere, the heat may accelerate the denaturation of non-volatile residues and cause off-odors. There are drawbacks such as the non-volatile residue significantly inhibiting the deodorizing and evaporation performance of the deodorizing material. Therefore, it has been proposed to further process the extract to minimize the amount of non-volatile residue, but to date, there has been little problem in using the non-volatile residue when forced evaporation is carried out. The actual situation was that no consideration had been given to reducing the number of items to a minimum so that they would not be left behind. [Means for Solving the Problems] In view of the above-mentioned circumstances, an object of the present invention is to provide a deodorizing and deodorizing material containing plant components and producing less non-volatile residue, which can eliminate these drawbacks. It was created as a mother liquor, which is made from the leaves of plants such as evergreen broad-leaved trees, which are first treated with solvent extraction, and then this first treated mother liquor is further heated under atmospheric pressure at a temperature of 130℃ or less. It is characterized in that the active ingredient is a secondary treatment component that is distilled at a high temperature and that when the distillate component is heat-treated and forcibly evaporated, the amount of non-volatile residue is minimal. It is something. With this configuration, the present invention is a deodorizing and deodorizing material that contains plant components collected from plants such as evergreen broad-leaved trees, but it is possible to eliminate non-volatile residues that cause off-odor in the material itself. It is designed so that it does not include The plants used in the present invention include tea,
The leaves of commonly known plants such as camellia, camellia, sasanqua, camphor tree, laurel, and sakaki are used as materials, and these can be used alone or in combination. semi-dried food,
It may also be dried. Furthermore, methyl alcohol, ethyl alcohol, n-
propyl alcohol, isopropyl alcohol,
n-butyl alcohol, diethylene glycol,
Lower alcohol solvents such as propylene glycol, ketone solvents such as acetone and methyl ethyl ketone, ether solvents such as diethyl ether, dioxane, and tetrahydrofuran can be used alone or as a mixture of a plurality of solvents, and further as a mixed solvent with water. . Then, solvent extraction is performed by refluxing the plant materials such as evergreen broad-leaved trees in a solvent, or heating and stirring in a solvent, and extraction processing is performed by filtration or vacuum distillation to separate the raw material residue. ,
As a result, a primary treated mother liquor is obtained. This mother liquor is further subjected to secondary treatment by distillation under atmospheric pressure. In addition, the present invention has a temperature of approximately 130°C or lower (preferably 120°C or lower).
It contains as an active ingredient a distillation component that is distilled at a temperature of up to Odor and deodorizing materials can contain the solvent that is distilled together as an active ingredient, but
Furthermore, the product from which the solvent has been removed can be used as an active ingredient in deodorizing and deodorizing materials. At this time, when removing the solvent, if the boiling point of the solvent is below the upper limit temperature of distillation, and if the boiling point is considerably lower than the upper limit temperature of distillation, when distilling the mother liquor,
After the low-boiling point solvent is distilled off, the distilled component that is distilled out at a temperature between the boiling point of the solvent and the upper limit temperature of distillation can be collected as an active ingredient for deodorizing and deodorizing materials. If the temperature is close to the upper limit temperature, the solvent and the effective components of the deodorizing and deodorizing material can be separated from the solvent by means such as vacuum distillation of what is distilled out together with the solvent. In addition, in the case of a solvent with a boiling point above the upper limit temperature of distillation, the mother liquor is distilled as it is under atmospheric pressure, and the distilled component distilled at a temperature below the upper limit temperature of distillation is used as a deodorizing and deodorizing material containing almost no solvent. It is the active ingredient of It goes without saying that the active ingredients of the deodorizing and deodorizing materials obtained in this way can be used alone or in combination with other deodorizing and deodorizing materials. The liquid material containing the deodorizing and deodorizing material of the present invention as an active ingredient can be used in a general manner, such as by diluting it with an appropriate solvent or spraying it as an aerosol. A suction medium formed using a capillary tube assembly, a glass mat, etc. is filled in a tank provided so as to protrude, and by heating the suction medium, the extinguishing agent sucked up through the suction medium is heated. It can also be used in a deodorizing device configured to forcibly evaporate odor and deodorizing materials into the atmosphere. [Effects] Since the present invention is constructed as described above, the active ingredients of deodorizing and deodorizing materials containing plant components obtained from the leaves of plants such as evergreen broad-leaved trees and having little non-volatile residue are , which was first treated by solvent extraction, and then further processed at atmospheric pressure for 130°C.
Since the active ingredient is obtained through secondary treatment by distillation at a temperature below ℃, the main ingredient is something that easily vaporizes, and it is an extremely volatile substance with no distillation residue. It will be composed by. By ensuring that the distillation temperature during secondary treatment does not exceed 130°C, aromatic substances such as flavone-based substances, unsaturated aldehydes, unsaturated carboxylic acids, or benzaldehyde that volatilize at higher temperatures can be removed. Highly non-volatile substances such as group compounds that change easily over time and cause off-odors are extremely small and are hardly contained in the ingredients. If you try to use it by forcing evaporation inside the tank, as with conventional products, a large amount of non-volatile residue will remain in the tank, or non-volatile substances will accumulate in the heating part and cause clogging. This product provides excellent deodorization and deodorization over a long period of time, without causing early deterioration in the wicking properties of the liquid material or by heating, which promotes the denaturation of non-volatile substances and causing them to warp and emit strange odors. Performance can be maintained. Hereinafter, the present invention will be explained in more detail with reference to Examples. Example 1 Using powdered dried leaves of tea plants as the leaves of plants such as evergreen broad-leaved trees, 150 g of this powder and 500 ml of ethanol were added.
and was placed in a Soxhlet extractor and heated under reflux for 24 hours. Then, the raw material residue is removed from the extract by filtration to obtain 545 g of primary treated mother liquor. This mother liquor is then placed in a round-bottomed flask equipped with a Liebig condenser and heated to distill. And by distilling substances up to a temperature of 130℃,
430g of deodorizing and deodorizing material as a secondary treated ethanol solution was obtained. Examples 2 and 3 Based on the same method as in Example 1, the mother liquor of the primary treatment was extracted using plants as shown in Table 1,
This mother liquor was further distilled and subjected to secondary treatment to obtain the deodorizing and deodorizing material of the present invention. Examples 4 and 5 A mother liquor was obtained based on the same method as in Example 1, and this mother liquor was further subjected to distillation treatment. In this case, the solvent was first distilled off as a distillate component up to its boiling point temperature, and then the solvent From temperatures above the boiling point
The active ingredients distilled at temperatures up to 120°C or 130°C were collected. The results are shown in Table 1. Comparative Example 1 The mother liquor was produced according to the same recipe as in Example 2, but the fractional distillation temperature in the secondary treatment of the mother liquor was increased to 150° C., and 490 g of distilled components were collected.
【表】【table】
【表】
検討例 1
そしてこの様にして得られた各消臭、脱臭材を
用いて異臭の発生状況を比較検討した。この実験
に供する器機としては、500ml入りの液材タンク
に、実施例1、3については、採取された消臭、
脱臭材の200mlを水にて450mlに希釈したものを入
れ、実施例2、比較例1、並びに実施例2の母液
(以下このものを比較例2と称する)については、
これらそのままをそれぞれ450mlずつ入れ、また
実施例4、5については、採取された消臭、脱臭
材の20gを10%プロピレングリコールにて450ml
となるように希釈したものを入れた。そしてこの
各液材タンクに編組された親水性のガラスマツト
を差し込んでタンク内の液材を吸い上げることが
できるようにし、さらにガラスマツトの液材タン
クから突出した部位には、ガラスマツト部の温度
が略200℃に維持されるように温度調節するヒー
タを設け、ガラスマツトから加熱により強制的に
蒸散される消臭、脱臭材の臭いを逐次観測し、そ
の結果、並びに7日後に液材タンク内に残留する
残燔量の測定結果について表2に示す。[Table] Study Example 1 Using each of the deodorizing and deodorizing materials obtained in this manner, the occurrence of off-odor was compared and studied. The equipment used for this experiment was a 500ml liquid tank, and for Examples 1 and 3, the sampled deodorizer,
Add 200 ml of deodorizing material diluted to 450 ml with water, and for the mother liquor of Example 2, Comparative Example 1, and Example 2 (hereinafter referred to as Comparative Example 2),
Pour 450 ml of each of these directly, and for Examples 4 and 5, add 20 g of the collected deodorizing and deodorizing material to 450 ml of 10% propylene glycol.
I diluted it so that it was. A braided hydrophilic glass mat is inserted into each liquid material tank so that the liquid in the tank can be sucked up, and the temperature of the glass mat part is approximately 200℃. A heater was installed to adjust the temperature to maintain the temperature at ℃, and the odor of the odor and deodorizing material forcibly evaporated from the glass mat by heating was sequentially observed. Table 2 shows the measurement results of the amount of residual soot.
【表】
この様に、消臭、脱臭器を用い、植物成分を含
有する不揮発性残渣物の少ない消臭、脱臭材を加
熱によつて強制的に蒸散させた場合に、本発明を
実施したものは何れのものも、蒸散される物質か
らは3日後までは異臭がなく、5日後において僅
かに異臭を発するものがあつた。しかしながら実
用には殆ど問題にならない程度の僅かなものであ
つた。これに対して、比較例1、2のものは、1
時間後で既に何れも僅かに異臭を発している。そ
して両者共、時間の経過に伴い異臭が強くなつて
くるが、この臭いは、茶の焦げた様な鼻をつく異
様な臭いであつて、とても耐えることができない
ものである。そして7日後においては、本発明を
実施した消臭、脱臭材は、液材の蒸散が何れも終
了しており、そして残渣も極めて僅かしかない
が、比較例1、2のものは多量の残渣を残してい
ることが判明し、そして残渣量について、二次処
理の際の蒸留温度が130℃までと150℃までと異な
るのみで、それ以外は全く同じ条件である実施例
2のものと比較例1のものとを対比したときに、
残渣量が0.3gと25.8gと、単純計算でも86倍も
の大きな差が認められ、本発明が如何に有効であ
るかが判明する。まして二次処理をしていない比
較例2に至つては、ガラスマツトに茶褐色をした
物質が大量にこびり付いており、しかもここから
異臭が発生し、そのうえ最早タンク内の液材の吸
い上げも成されていない状態であつた。
検討例 2
さらに前記実施例1、2と比較例1、2とで採
取した消臭、脱臭材についての消臭、脱臭性の検
討をした。それには500mlのフラスコにアンモニ
アガスを濃度が200ppmとなるように注入し、こ
こに各消臭、脱臭材の3mlを素早く充填し、10分
後におけるフラスコ内の残存アンモニア濃度を北
川式の検知管によつて測定したが、何れのものも
アンモニア濃度は検出下限未満であり、これによ
つて本発明の消臭、脱臭材における消臭、脱臭性
能は、蒸留処理しない従来のものと遜色ないとい
うことが判明する。また、これとは別に、実施例
2のものにおいて、120℃〜150℃の温度範囲で蒸
留する液材を採取しておき、このものを上記手順
に従つて残存アンモニアガスの濃度を調べたとこ
ろ、その濃度は10ppmであつた。因みに蒸留水を
用いたブランク実験で同じく残存アンモニアガス
濃度を調べたところ12ppmであつた。
これらのことから、本発明の蒸留処理した消
臭、脱臭材は優れた消臭、脱臭性を有するもので
あることが判るが、さらに上記高温度範囲におけ
る蒸留成分のものは、消臭、脱臭性があまり芳し
くないことから、消臭、脱臭材として真に有効な
成分は本発明の温度範囲において蒸留する留分に
殆ど含まれ、それ以上の温度での留分は、実質的
に消臭、脱臭材としてあまり有効に作用しないも
のであると言え、消臭、脱臭材を加熱して強制的
に蒸散させようとしたとき異臭を発しないため、
常緑広葉樹の葉から抽出した母液を大気圧下で略
130℃を限界として留出した成分を有効成分とし
たことは、偶然にも常緑広葉樹等の植物の葉から
抽出した母液から、消臭、脱臭性に有効な成分を
分離抽出していることを意味していることが興味
深いものである。[Table] In this way, the present invention was carried out when a deodorizing and deodorizing device was used to forcibly evaporate the deodorizing and deodorizing material containing plant components with a small amount of non-volatile residue by heating. In all cases, there was no off-odor from the evaporated substances until 3 days later, and some gave off a slight off-odor after 5 days. However, the amount was so small that it hardly caused a problem in practical use. On the other hand, in Comparative Examples 1 and 2, 1
After some time, they were all already emitting a slight odor. In both cases, the odor becomes stronger as time passes, but this odor is like burnt tea and is very unpleasant to the nose. After 7 days, the deodorizing and deodorizing materials according to the present invention have completely evaporated the liquid and have very little residue, but those of Comparative Examples 1 and 2 have a large amount of residue. The amount of residue was compared with that of Example 2, where the only difference was that the distillation temperature during the secondary treatment was up to 130°C and up to 150°C, and the other conditions were exactly the same. When compared with Example 1,
The amount of residue is 0.3 g and 25.8 g, which is a large difference of 86 times even by simple calculation, which shows how effective the present invention is. Moreover, in Comparative Example 2, in which secondary treatment was not performed, a large amount of brownish substance was stuck to the glass mat, and a strange odor was generated from this, and furthermore, the liquid material in the tank was no longer being sucked up. It was in a state where there was no. Study Example 2 Further, the deodorizing and deodorizing properties of the deodorizing and deodorizing materials collected in Examples 1 and 2 and Comparative Examples 1 and 2 were investigated. To do this, inject ammonia gas into a 500 ml flask to a concentration of 200 ppm, quickly fill it with 3 ml of each deodorizing agent, and measure the remaining ammonia concentration in the flask after 10 minutes using a Kitagawa detection tube. The ammonia concentration in all cases was below the detection limit, which indicates that the deodorizing and deodorizing performance of the deodorizing material of the present invention is comparable to that of conventional materials that are not subjected to distillation treatment. It turns out that. Separately, in Example 2, the liquid material to be distilled at a temperature range of 120°C to 150°C was collected, and the concentration of residual ammonia gas was examined using this material according to the above procedure. , its concentration was 10 ppm. Incidentally, when the residual ammonia gas concentration was also investigated in a blank experiment using distilled water, it was 12 ppm. These results indicate that the distilled deodorizing and deodorizing material of the present invention has excellent deodorizing and deodorizing properties. Since the properties are not very good, most of the ingredients that are truly effective as deodorizing and deodorizing materials are contained in the fraction distilled within the temperature range of the present invention, and the fraction distilled at a temperature higher than that is substantially deodorizing. It can be said that it does not work very effectively as a deodorizing material, as it does not emit any strange odor when trying to forcefully evaporate it by heating the deodorizing material.
The mother liquor extracted from the leaves of evergreen broad-leaved trees is extracted under atmospheric pressure.
The fact that the active ingredients were distilled at a temperature of 130 degrees Celsius coincidentally means that the ingredients effective in deodorizing and deodorizing properties are separated and extracted from the mother liquor extracted from the leaves of plants such as evergreen broad-leaved trees. What it means is interesting.
Claims (1)
溶媒抽出で一次処理したものを母液とし、この一
次処理した母液をさらに大気圧下にて130℃以下
の範囲の温度で留出させて、その留出成分が加熱
処理されて強制的に蒸散気化せしめたときの不揮
発性残渣物が僅少になるようにした二次処理成分
を有効成分としていることを特徴とする植物成分
を含有する不揮発性残渣物の少ない消臭、脱臭
材。 2 素材の溶媒抽出に使用する溶媒としては、沸
点が略130℃以下のものであるとし、溶媒と共に
130℃以下の温度で留出する蒸留成分をそのまま
有効成分としていることを特徴とする特許請求の
範囲第1項記載の植物成分を含有する不揮発性残
渣物の少ない消臭、脱臭材。 3 素材の溶媒抽出に使用する溶媒としては、沸
点が略130℃以下のものであるとし、略130℃以下
の温度で留出した蒸留成分には溶媒が留去された
ものを有効成分としていることを特徴とする特許
請求の範囲第1項記載の植物成分を含有する不揮
発性残渣物の少ない消臭、脱臭材。 4 素材の溶媒抽出に使用する溶媒としては、沸
点が略130℃以上のものであるとし、溶媒抽出さ
れたものは減圧蒸留して母液とし、この母液を大
気圧下にて蒸留し、130℃以下の温度で留出する
蒸留成分を有効成分としていることを特徴とする
特許請求の範囲第1項記載の植物成分を含有する
不揮発性残渣物の少ない消臭、脱臭材。[Scope of Claims] 1. A mother liquor is obtained by first treating leaves of plants such as evergreen broad-leaved trees with solvent extraction, and further treating this first-treated mother liquor at a temperature in the range of 130°C or less under atmospheric pressure. A plant ingredient characterized in that its active ingredient is a secondary-treated ingredient that is distilled and the distilled ingredient is heat-treated to forcibly evaporate, leaving only a small amount of non-volatile residue. A deodorizing and deodorizing material containing less non-volatile residue. 2 The solvent used for solvent extraction of the material must have a boiling point of approximately 130℃ or less, and should be used together with the solvent.
The deodorizing and deodorizing material containing plant components and having little non-volatile residue as claimed in claim 1, characterized in that the distillation component distilled at a temperature of 130° C. or lower is used as an active ingredient. 3 The solvent used for solvent extraction of the material must have a boiling point of approximately 130°C or lower, and the distilled component distilled at a temperature of approximately 130°C or lower is the active ingredient from which the solvent has been distilled off. A deodorizing and deodorizing material containing a plant component as claimed in claim 1 and having a small amount of non-volatile residue. 4. The solvent used for solvent extraction of the material should have a boiling point of approximately 130°C or higher, and the solvent extracted should be distilled under reduced pressure to obtain a mother liquor, and this mother liquor should be distilled under atmospheric pressure and heated to 130°C. The deodorizing and deodorizing material containing plant components and having little non-volatile residue as claimed in claim 1, characterized in that the effective ingredient is a distillation component that is distilled out at a temperature of:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62265889A JPH01107767A (en) | 1987-10-21 | 1987-10-21 | Deodorant containing vegetable ingredient |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62265889A JPH01107767A (en) | 1987-10-21 | 1987-10-21 | Deodorant containing vegetable ingredient |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01107767A JPH01107767A (en) | 1989-04-25 |
| JPH0362099B2 true JPH0362099B2 (en) | 1991-09-24 |
Family
ID=17423506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62265889A Granted JPH01107767A (en) | 1987-10-21 | 1987-10-21 | Deodorant containing vegetable ingredient |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01107767A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0311020A (en) * | 1989-06-08 | 1991-01-18 | Shiraimatsu Shinyaku Kk | Odor-destroying and deodorizing material containing plant components |
| JPH04114985A (en) * | 1990-08-31 | 1992-04-15 | Mitsui Norin Kk | Production of odorless compost composed of livestock manure or fish meal and a composition containing polyphenol component |
| JP4878352B2 (en) * | 2008-03-26 | 2012-02-15 | 大日本除蟲菊株式会社 | Method of heat transpiration of aqueous deodorant composition |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56100060A (en) * | 1980-01-14 | 1981-08-11 | Shiraimatsu Shinyaku Co | Deodorant composition |
| JPS5861751A (en) * | 1981-10-09 | 1983-04-12 | 白井松新薬株式会社 | Deodrant preparation containing extract from camellia plant as available component |
| JPS6238165A (en) * | 1985-08-13 | 1987-02-19 | 株式会社 ココノエ | Deodorizing composition |
-
1987
- 1987-10-21 JP JP62265889A patent/JPH01107767A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01107767A (en) | 1989-04-25 |
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