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JPS6229056B2 - - Google Patents
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JPS6229056B2 - - Google Patents

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Publication number
JPS6229056B2
JPS6229056B2 JP58124161A JP12416183A JPS6229056B2 JP S6229056 B2 JPS6229056 B2 JP S6229056B2 JP 58124161 A JP58124161 A JP 58124161A JP 12416183 A JP12416183 A JP 12416183A JP S6229056 B2 JPS6229056 B2 JP S6229056B2
Authority
JP
Japan
Prior art keywords
fragrance
film
solid particles
binder
fragrance composition
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
Application number
JP58124161A
Other languages
Japanese (ja)
Other versions
JPS6016914A (en
Inventor
Shigehiro Nagura
Noboru Aiba
Michio Aizawa
Akira Yamamoto
Tooru Chiba
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical 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 Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP58124161A priority Critical patent/JPS6016914A/en
Priority to CA000456814A priority patent/CA1244343A/en
Priority to AU29471/84A priority patent/AU566939B2/en
Priority to EP19840107132 priority patent/EP0131783B1/en
Priority to BR8403042A priority patent/BR8403042A/en
Priority to DE8484107132T priority patent/DE3479698D1/en
Publication of JPS6016914A publication Critical patent/JPS6016914A/en
Publication of JPS6229056B2 publication Critical patent/JPS6229056B2/ja
Granted legal-status Critical Current

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  • Cosmetics (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Fats And Perfumes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は改良された徐放性香料組成物およびそ
の製造方法に関するものである。 一般に香料(防臭剤を包含する)は揮発性のも
のであつてその効果は一時的であるため、香料を
長時間にわたつて徐々に放出させる工夫が種々試
みられている。 従来の芳香剤としては、香料液を直接霧状飛散
させる方法、基材にゴム質やシリカゲル、活性炭
等を用い香料を固形状とし室温または加熱下でき
揮散させる方法、香料を開放部分面積を制限した
容器中に収納する方法、昇華性物質中に香料を分
散させて昇華性物質とともに揮散させる方法等が
提案されている。 しかしこれらの方法は香料を揮散させるための
特別な装置が必要となつたり、芳香の持続性が不
充分であつたり、粒状のように小型化した香料組
成物は得られないなどの欠点がある。 また最近は粒状活性アルミナに調合香料を保持
させた後、その表面を通気性のあるセルローズ化
合物の薄膜で被覆した粒状発香体(特公昭56−
7423号公報)、あるいはまた吸湿性の吸着剤に香
料を吸着せしめ、ついで成形し、さらに加熱によ
り香料が揮散する程度に高分子コーテイング剤で
被覆した芳香錠剤(特開昭53−69840号公報)が
提案されている。 しかしながら、前者は香料の初期の放出速度が
大きくなる傾向があり充分に放出制御されない
し、製造時の香料のロスが多い。また後者は室温
では香料が放出されないという欠点がある。 本発明は従来のかかる技術的課題に鑑み鋭意研
究の結果完成されたもので、これは香料を吸着し
た不活性担体粉末を結合剤により造粒してなる固
形粒子の全表面を、フイルム形成性重合体または
フイルム形成性重合体と無機質粉末との混合物か
らなる、香料に対し透過性を有する連続層状の被
膜層で被覆してなり、該香料と不活性担体との重
量比率が1:0.3〜1:10、不活性担体と結合剤
との重量比率が1:0.1〜1:3、フイルム形成
性重合体と無機質粉末との重量比率が1:0〜
1:4である徐放性香料組成物およびその製造方
法に関するものである。 この本発明によれば、従来のものに見られない
芳香保持性を有し、必要に応じ容易に粒状のよう
な小型化した発香体を得ることができる。さらに
は不活性担体の量、結合剤の量、粒の表面積、被
膜の厚さなどを変化させることにより香料の放出
速度を設定することが可能である。したがつて蒸
気圧の異なる香料成分を本発明によりそれぞれ放
出速度を設定した香料組成物となし、その後混
合、調合することにより、放出の初期から末期に
いたるまでの香りの変化なしに安定な調合された
芳香を供することができる。また本発明の香料組
成物の製造方法は製造時における香料のロスを少
なく抑え、香料の放出速度の設定を容易に可能と
する利点があり、低コストの工業的な製造方法で
ある。 本発明で対象とされる香料としては、単一の成
分でもよいしあらかじめ調合された香料を使用す
ることもできる。なお、香料と共に必要に応じ香
料安定剤が使用されるが、この場合の香料安定剤
としては紫外線吸収剤や抗酸化剤から適当なもの
が選択される。 不活性担体としては香料を良好に吸着ないし吸
収担持し香料に対して不活性であるものが望まし
く、これには無水けい酸、各種けい酸塩、タルク
などの無機質粉末、およびセルロース粉末、でん
ぷんなどの多糖類や多糖類誘導体などの有機質粉
末が例示される。 また、結合剤としては、でんぷん、プルラン、
ザンタンガムなどの多糖類、セルロース誘導体な
どの多糖類誘導体、ポリアミド、ポリエステル、
ポリエーテル、ビニル系ポリマーなどの合成高分
子が例示されるが、とくには香料と相溶する溶媒
に溶解する結合剤が好適とされる。 フイルム形成性重合体としては生成された被膜
が香料を適度に透過させるものであることが必要
で、これにはでんぷん、プルラン、ザンタンガム
などの多糖類、セルロース誘導体などの多糖類誘
導体、ポリアミド、ポリエステル、ポリエーテ
ル、ビニル系ポリマーなどの合成高分子などが例
示される。これらのうちでも沸点が120℃以下の
溶媒に溶解するフイルム形成性重合体が好適とさ
れる。しかして、このフイルム形成性重合体には
必要に応じ無機質粉末が混合使用されてもよく、
これによれば被膜層を透過する香料の放出速さの
コントロールが一層容易となる効果が与えられ
る。このような目的で使用される無機質粉末とし
ては無水けい酸、各種けい酸塩、タルクなどが例
示される。なお、このフイルム形成性重合体には
造膜助剤としてステアリン酸などのワツクス類を
併用してもよい。 前記した結合剤およびフイルム形成性重合体と
しては天然もしくは合成の高分子物質が使用され
るが、これらのうちでも特にバクテリアや酵素に
より分解されるものであつて天然界に蓄積されな
いものを選択することが望ましい。 本発明の徐放性香料組成物は、以上記載した香
料、香料安定剤、不活性担体、結合剤、フイルム
形成性重合体、無機質粉末等から構成されるが、
徐放性という本発明の目的を達成する見地からは
これら各成分の使用割合を次のとおりとすること
が望ましい。なお、各成分はそれぞれ1種類ずつ
に限定されるものではなく、同一範ちゆうの成分
を2種以上併用することは何ら差支えない。 固形粒子 香 料 0.5〜60重量% 香料安定剤 0〜6 〃 不活性担体 10〜50 〃 結 合 剤 1〜30 〃 被膜層 フイルム形成性重合体 5〜50 〃 無機質粉末 0〜30 〃 以上の各範囲内で総計100%となる組合せの組
成であることが望ましく、しかも前記したよう
に、香料と不活性担体との重量比率が1:0.3〜
1:10、不活性担体と結合剤との重量比率が1:
0.1〜1:3、被覆層におけるフイルム形成性重
合体と無機質粉末との比率が1:0〜1:4の組
成となるように選択することが必要である。香料
の含有率が0.5重量%未満では香料の放出速度が
きわめて小さくなり芳香効果が発揮されないし、
一方香料含有率が60%を越えるものでは製造時の
香料のロスが多くなり、また放出速度の制御が困
難となるなどの不都合が生じる。他方結合剤が1
%未満となるような組成では製造時における香料
の蒸発ロスが大きくなる。 いずれにしても、香料、不活性担体、結合剤、
フイルム形成性重合体、無機質粉末の適当な比率
を選定することにより香料の放出速さを望ましい
値に設定することができる。 本発明の徐放性香料組成物はまず香料を吸着し
た不活性担体粉末を香料と相溶する溶媒に溶解し
た結合剤溶液を用いて造粒したのち乾燥して固形
粒子となし、(イ)この固形粒子を流動状態に保持し
ながら、その全表面にフイルム形成性重合体の沸
点120℃以下の溶媒溶液またはこれの無機質粉末
との混合溶液を噴霧し乾燥させるか、(ロ)固形粒子
にフイルム形成性重合体の前記溶媒溶液を添加し
て、その全表面をコーテイングし、これに無機質
粉末を加えて粒状に保ち、ついで乾燥させる方法
によつて製造される。 これに更に詳細に説明すると、まず混合機に香
料と不活性担体とさらに要すれば香料安定剤とを
仕込み混合することにより、香料を不活性担体に
吸着させる。このときより均一な混合を達成する
ために香料を適当な有機溶媒で希釈してもよい。
つぎに結合剤の溶媒溶液を添加し混練するかまた
は結合剤を粉末状で添加混合した後これに結合剤
の溶媒を加えて混練し、適当な粒状化装置を用い
て望ましくは平均粒子径0.3〜10mmの粒状物(固
形粒子)とする。この際使用される結合剤の溶媒
は香料と相溶性を有するものであることが必要
で、香料と相溶性のない溶媒を使用すると、粒状
化の際に香料が粒子表面から遊離することがあり
不都合である。 つぎに、このようにして製造した固形粒子の表
面をフイルム形成性重合体またはフイルム形成性
重合体と無機質粉末との混合物で被膜層を形成す
るのであるが、前記(イ)の方法における固形粒子の
流動条件下における被覆操作は、固形粒子の温度
が低温条件下で行なわれることが望ましく、具体
的には5℃〜50℃の範囲の温度条件下で行われる
ことが好ましい。この温度が高すぎると噴霧操作
中の香料の蒸発ロスが多くなり不都合であるし、
また逆に低すぎると噴霧液の溶媒の蒸発が著しく
遅くなり粒子同志が粘着を起すようになつて均一
な被覆が行なわれなくなる。なお、フイルム形成
性重合体の溶媒としては沸点120℃以下のものを
使用することが必要で、この溶媒が沸点120℃よ
りも高いものでは蒸発が遅いため粒子同志の粘着
が起こり易くなり、またこのような場合には溶媒
の蒸発を促進するために上記固形粒子の温度を50
℃以上に設定する必要が生じ香料の蒸発ロスが多
くなるという不都合が生じる。 また噴霧液におけるフイルム形成性重合体の濃
度は、通常0.5〜10重量%の範囲とすることが好
ましい。この噴霧液には必要に応じ無機質粉末が
前記した範囲内で懸濁添加されるが、これによれ
ば香料の放出速さを適度な大きさに設定すること
が容易となるほか、噴霧操作中における粒子同志
の粘着が起こりにくくなり、均一な被膜層が形成
されるばかりでなく、被覆操作時の粒子温度を比
較的低温条件下で行うことが可能となる。(ロ)の方
法においても被膜層中に無機質粉末を含有させる
ことにより香料の放出速さを適度な大きさに設定
することが容易となる。なお、この乾燥は必要に
応じ、流動条件下で行なうこともできる。 つぎに具体的実施例をあげる。 実施例 1 軟質無水けい酸(日本アエロジル社製商品名ア
エロジル)30重量部に、α―リモネン30重量部を
混合し、つぎに結合剤としてセルロースアセテー
ト(ダイセル化学社製商品名L―20)の塩化メチ
レン/エタノール(9/1重量比)系5%溶液
180重量部を添加混練し、公知の押出顆粒装置に
より顆粒化し、平均粒径1mmの球形および円柱形
の素顆粒を得た。 つぎに、この素顆粒にエチルセルロース(ダ
ウ・ケミカル社製商品名エトセル・スタンダー
ド)のエタノール/トルエン(8/2重量比)系
4%溶液を流動装置中で45℃の空気を流動媒体と
してスプレーコーテイングし、素顆粒に対し30重
量%の被膜を形成した。 得られた香料組成物をアセトンに溶解抽出し、
ラウリン酸メチルを内部標準としてガスクロマト
グラフイーで分析したところ、全体の重量に対し
32.0重量%のα―リモネンが含有されていた。 つぎに、この香料組成物313mgを30℃、風速
0.5m/秒の条件下に置き、α―リモネンの放出
量を重量変化と内部標準ガスクロマトグラフイー
で定量分析しながら測定したところ、第1表に示
すとおりの結果を得た。 実施例 2 実施例1で得た素顆粒を使用し、また実施例1
と同様にエチルセルロースをスプレーコーテイン
グし、素顆粒に対し40重量%の被膜を形成した。
得られた香料組成物を実施例1と同様に分析した
ところ、全体の重量に対し30.1重量%のα―リモ
ネンが含有されていた。つぎにこの香料組成物
332mgについて実施例1と同様にα―リモネンの
放出量を測定したところ、第1表に示すとおりの
結果を得た。 実施例 3 軽質無水けい酸30重量部に、α―リモネン30重
量部を混合し、つぎに結合剤としてセルロースア
セテートの塩化メチレン/エタノール(9/1重
量比)系10%溶液180重量部を添加混練し、実施
例1と同様の操作で素顆粒を得た。つぎにこの素
顆粒に実施例1と同様にエチルセルロースをスプ
レーコーテイングし素顆粒に対し40重量%の被膜
を形成した。得られた香料組成物を実施例1と同
様に分析したところ、全体の重量に対し27.0重量
%のα―リモネンが含有されていた。つぎにこの
香料組成物370mgについて実施例1と同様にα―
リモネンの放出量を測定したところ、第1表に示
すとおりの結果を得た。
TECHNICAL FIELD This invention relates to improved sustained release perfume compositions and methods for producing the same. Generally, fragrances (including deodorants) are volatile and their effects are temporary, so various attempts have been made to gradually release fragrances over a long period of time. Conventional fragrances include methods in which the fragrance liquid is directly dispersed in the form of a mist, methods in which the fragrance is solidified using rubber, silica gel, activated carbon, etc. as a base material and volatilized at room temperature or under heat, and methods in which the open area of the fragrance is limited. There have been proposed methods such as storing the perfume in a sublimable container and dispersing the perfume in a sublimable substance and volatilizing it together with the sublimable substance. However, these methods have drawbacks such as requiring special equipment to volatilize the fragrance, insufficient persistence of the fragrance, and the inability to obtain a compact fragrance composition such as granules. . In addition, recently, granular fragrance materials (Special Publications 1983-1983-1) have been developed, in which granular activated alumina is made to hold a blended fragrance, and then its surface is coated with a thin film of an air-permeable cellulose compound.
7423), or aromatic tablets in which fragrance is adsorbed on a hygroscopic adsorbent, then molded, and coated with a polymeric coating agent to such an extent that the fragrance evaporates upon heating (Japanese Patent Laid-Open No. 53-69840). is proposed. However, in the former case, the initial release rate of the fragrance tends to be high, the release is not sufficiently controlled, and there is a lot of loss of the fragrance during production. The latter also has the disadvantage that fragrance is not released at room temperature. The present invention was completed as a result of intensive research in view of the conventional technical problems, and it is made by granulating inert carrier powder adsorbed with fragrance using a binder. It is coated with a continuous layer-like coating layer made of a mixture of a polymer or a film-forming polymer and an inorganic powder and is permeable to the fragrance, and the weight ratio of the fragrance and the inert carrier is 1:0.3 to 0.3. 1:10, the weight ratio of the inert carrier to the binder is 1:0.1 to 1:3, and the weight ratio of the film-forming polymer to the inorganic powder is 1:0 to 1:0.
The present invention relates to a sustained release fragrance composition with a ratio of 1:4 and a method for producing the same. According to the present invention, it is possible to easily obtain a compact, granular fragrance body as required, which has aroma retention properties not found in conventional products. Furthermore, by varying the amount of inert carrier, the amount of binder, the surface area of the particles, the thickness of the coating, etc., it is possible to set the release rate of the perfume. Therefore, according to the present invention, perfume components with different vapor pressures are made into a perfume composition with respective release rates set, and then mixed and formulated, it is possible to create a stable formulation without any change in fragrance from the initial stage to the final stage of release. It can provide a unique aroma. Furthermore, the method for producing a fragrance composition of the present invention has the advantage of minimizing the loss of fragrance during production and making it possible to easily set the release rate of the fragrance, and is a low-cost industrial manufacturing method. The fragrance targeted by the present invention may be a single component or may be a pre-mixed fragrance. Incidentally, a fragrance stabilizer is used along with the fragrance if necessary, and in this case, a suitable fragrance stabilizer is selected from ultraviolet absorbers and antioxidants. The inert carrier is preferably one that adsorbs or absorbs the fragrance well and is inert to the fragrance, such as inorganic powders such as silicic anhydride, various silicates, and talc, cellulose powder, and starch. Examples include organic powders such as polysaccharides and polysaccharide derivatives. In addition, as binders, starch, pullulan,
Polysaccharides such as xanthan gum, polysaccharide derivatives such as cellulose derivatives, polyamides, polyesters,
Synthetic polymers such as polyether and vinyl polymers are exemplified, but binders that are soluble in solvents that are compatible with perfumes are particularly preferred. For film-forming polymers, it is necessary that the resulting film is moderately permeable to fragrances, and this includes polysaccharides such as starch, pullulan, and xanthan gum, polysaccharide derivatives such as cellulose derivatives, polyamides, and polyesters. Examples include synthetic polymers such as , polyether, and vinyl polymers. Among these, film-forming polymers that dissolve in solvents with a boiling point of 120° C. or lower are preferred. Therefore, an inorganic powder may be mixed with this film-forming polymer if necessary.
According to this, it is possible to more easily control the rate of release of the fragrance that passes through the coating layer. Examples of inorganic powders used for this purpose include silicic anhydride, various silicates, and talc. Incidentally, waxes such as stearic acid may be used in combination with this film-forming polymer as a film-forming agent. Natural or synthetic polymeric substances can be used as the above-mentioned binder and film-forming polymer, but among these, those that are decomposed by bacteria or enzymes and are not accumulated in nature are selected. This is desirable. The sustained release fragrance composition of the present invention is composed of the fragrance described above, a fragrance stabilizer, an inert carrier, a binder, a film-forming polymer, an inorganic powder, etc.
From the viewpoint of achieving the objective of the present invention, which is sustained release, it is desirable that the proportions of these components used are as follows. Note that each component is not limited to one type each, and there is no problem in using two or more types of components in the same category in combination. Solid particle fragrance 0.5-60% by weight Perfume stabilizer 0-6 〃 Inert carrier 10-50 〃 Binder 1-30 〃 Coating layer film-forming polymer 5-50 〃 Inorganic powder 0-30 〃 Each of the above It is desirable that the composition is a combination that makes up a total of 100% within the range, and as mentioned above, the weight ratio of fragrance and inert carrier is 1:0.3 to 1:0.3.
1:10, the weight ratio of inert carrier to binder is 1:1.
It is necessary to select the composition so that the ratio of the film-forming polymer to the inorganic powder in the coating layer is 0.1 to 1:3 and 1:0 to 1:4. If the fragrance content is less than 0.5% by weight, the release rate of the fragrance will be extremely low and the fragrance effect will not be exhibited.
On the other hand, if the fragrance content exceeds 60%, there will be a lot of fragrance loss during production, and there will be problems such as difficulty in controlling the release rate. On the other hand, the binder is 1
If the composition is less than %, the evaporation loss of the fragrance during production will be large. In any case, fragrance, inert carrier, binder,
By selecting an appropriate ratio of the film-forming polymer and the inorganic powder, the release rate of the fragrance can be set to a desired value. The sustained release fragrance composition of the present invention is prepared by first granulating an inert carrier powder adsorbing a fragrance using a binder solution dissolved in a solvent compatible with the fragrance, and then drying it to form solid particles, (a) While maintaining the solid particles in a fluid state, spray a solution of a film-forming polymer in a solvent with a boiling point of 120°C or less or a mixed solution of this with an inorganic powder onto the entire surface of the solid particles, or (b) dry the solid particles. It is manufactured by adding a solution of the film-forming polymer in the above-mentioned solvent to coat the entire surface thereof, adding an inorganic powder thereto to keep it in a granular form, and then drying it. To explain this in more detail, first, a fragrance, an inert carrier, and, if necessary, a fragrance stabilizer are charged and mixed in a mixer, so that the fragrance is adsorbed onto the inert carrier. At this time, the perfume may be diluted with a suitable organic solvent to achieve more uniform mixing.
Next, a solvent solution of the binder is added and kneaded, or after the binder is added and mixed in powder form, a solvent for the binder is added and kneaded, and the average particle size is preferably 0.3 using a suitable granulating device. ~10mm granules (solid particles). The binder solvent used at this time must be compatible with the fragrance; if a solvent that is not compatible with the fragrance is used, the fragrance may be liberated from the particle surface during granulation. It's inconvenient. Next, a coating layer is formed on the surface of the solid particles produced in this way with a film-forming polymer or a mixture of a film-forming polymer and an inorganic powder. The coating operation under flow conditions is preferably carried out under conditions where the temperature of the solid particles is low, and specifically preferably carried out under a temperature condition in the range of 5°C to 50°C. If this temperature is too high, there will be a lot of evaporation loss of fragrance during the spraying operation, which is inconvenient.
On the other hand, if it is too low, the evaporation of the solvent in the spray liquid will be extremely slow, particles will stick to each other, and uniform coating will not be achieved. In addition, it is necessary to use a solvent for the film-forming polymer with a boiling point of 120°C or lower; if the solvent has a boiling point higher than 120°C, evaporation is slow and particles tend to stick together. In such cases, the temperature of the solid particles may be increased to 50°C to promote evaporation of the solvent.
It is necessary to set the temperature above 0.degree. C., which causes the disadvantage that evaporation loss of fragrance increases. Further, the concentration of the film-forming polymer in the spray liquid is usually preferably in the range of 0.5 to 10% by weight. If necessary, inorganic powder is suspended and added to this spray liquid within the above-mentioned range, but this makes it easy to set the fragrance release rate to an appropriate level, and also makes it possible to This makes it difficult for the particles to stick together, and not only can a uniform coating layer be formed, but also allows the coating operation to be performed at a relatively low particle temperature. In the method (b) as well, by incorporating inorganic powder into the coating layer, it becomes easy to set the release rate of the fragrance to an appropriate level. Note that this drying can also be carried out under fluidized conditions, if necessary. Next, a specific example will be given. Example 1 30 parts by weight of soft silicic anhydride (trade name Aerosil, manufactured by Nippon Aerosil Co., Ltd.) was mixed with 30 parts by weight of α-limonene, and then cellulose acetate (trade name L-20, manufactured by Daicel Chemical Co., Ltd.) was added as a binder. 5% methylene chloride/ethanol (9/1 weight ratio) solution
180 parts by weight were added and kneaded and granulated using a known extrusion granulation device to obtain spherical and cylindrical elementary granules with an average particle diameter of 1 mm. Next, the elementary granules were spray coated with a 4% solution of ethyl cellulose (product name: Ethocel Standard, manufactured by Dow Chemical Company) in an ethanol/toluene (8/2 weight ratio) system in a fluidizer using air at 45°C as a fluidizing medium. Then, a coating of 30% by weight was formed on the elementary granules. The obtained fragrance composition is dissolved and extracted in acetone,
When analyzed by gas chromatography using methyl laurate as an internal standard, it was found that
It contained 32.0% by weight of α-limonene. Next, 313 mg of this fragrance composition was heated at 30°C and at a wind speed.
When placed under conditions of 0.5 m/sec and quantitatively analyzing the amount of α-limonene released by weight change and internal standard gas chromatography, the results shown in Table 1 were obtained. Example 2 The elementary granules obtained in Example 1 were used, and Example 1
Ethyl cellulose was spray coated in the same manner as above to form a coating of 40% by weight on the elementary granules.
When the obtained fragrance composition was analyzed in the same manner as in Example 1, it was found that it contained 30.1% by weight of α-limonene based on the total weight. Next, this fragrance composition
When the amount of α-limonene released was measured for 332 mg in the same manner as in Example 1, the results shown in Table 1 were obtained. Example 3 30 parts by weight of light silicic anhydride was mixed with 30 parts by weight of α-limonene, and then 180 parts by weight of a 10% solution of cellulose acetate in methylene chloride/ethanol (9/1 weight ratio) system was added as a binder. The mixture was kneaded and subjected to the same operation as in Example 1 to obtain elementary granules. Next, the elementary granules were spray coated with ethyl cellulose in the same manner as in Example 1 to form a coating of 40% by weight on the elementary granules. When the obtained fragrance composition was analyzed in the same manner as in Example 1, it was found that it contained 27.0% by weight of α-limonene based on the total weight. Next, α-
When the amount of limonene released was measured, the results shown in Table 1 were obtained.

【表】 第1表の各実施例のデータから、結合剤、フイ
ルム形成性物質の量を変化させることにより放出
速度を設定できることが確認された。 比較例 1 粉末状水酸化アルミニウムに、ヒドロキシプロ
ピルメチルセルロース(信越化学社製商品名TC
―5R)をバインダーとして、平均粒径2mmの球
形に造粒、活性化した活性アルミナ30重量部に、
α―リモネン10重量部を吸着させた後、エチルセ
ルロースのエタノール/トルエン(8/2重量
比)系6%溶液を実施例1と同様の条件でスプレ
ーコーテイングしたところ、残存α―リモネンは
初期含有量の43%にすぎず蒸発ロスが大きかつ
た。 実施例 4〜6 実施例1〜3に準じ、香料、不活性担体、結合
剤およびフイルム形成性重合体のそれぞれ種類お
よび含有量が第2表に示すとおりのものである徐
放性香料組成物を製造した。これらはいずれも良
好な徐放性を示すものであつた。第2表中の略記
号は下記のとおりの意味である。 (結合剤、フイルム形成性重合体の略称) HPMC=ヒドロキシプロピルメチルセルロース CA=セルロースアセテート PVA=ポリビニルアルコール HPC=ヒドロキシプロピルセルロース
[Table] From the data of each example in Table 1, it was confirmed that the release rate could be set by changing the amounts of the binder and film-forming substance. Comparative Example 1 Hydroxypropyl methylcellulose (product name: TC manufactured by Shin-Etsu Chemical Co., Ltd.) was added to powdered aluminum hydroxide.
-5R) as a binder, 30 parts by weight of activated alumina granulated and activated into spheres with an average particle size of 2 mm,
After adsorbing 10 parts by weight of α-limonene, a 6% solution of ethyl cellulose in ethanol/toluene (8/2 weight ratio) was spray coated under the same conditions as in Example 1. The evaporation loss was only 43%. Examples 4 to 6 Sustained-release fragrance compositions according to Examples 1 to 3, in which the types and contents of the fragrance, inert carrier, binder, and film-forming polymer are as shown in Table 2. was manufactured. All of these exhibited good sustained release properties. The abbreviations in Table 2 have the following meanings. (Abbreviation for binder, film-forming polymer) HPMC = Hydroxypropyl methyl cellulose CA = Cellulose acetate PVA = Polyvinyl alcohol HPC = Hydroxypropyl cellulose

【表】 実施例 7 軟質無水けい酸30重量部にα―リモネン30重量
部を混合し、つぎに結合剤としてセルロースアセ
テートの塩化メチレン/エタノール(9/1重量
比)系5%溶液180重量部を添加混練し、公知の
押出顆粒化装置により顆粒化し、平均粒径1mmの
球形および円柱形の素顆粒を得た。 つぎに、この素顆粒にエチルセルロースのエタ
ノール/トルエン(8/2重量比)系4%溶液
100重量部にタルク4重量部を懸濁した懸濁液
を、流動装置中で36℃の空気を流動媒体としてス
プレーコーテイングし、素顆粒に対し40重量%の
被膜を形成した。コーテイング操作中、粒子同志
の粘着は起こらず、良好なコーテイング操作が達
成された。 得られた香料組成物をアセトンに溶解抽出し、
ラウリン酸メチルを内部標準としてガスクロマト
グラフイーで分析したところ、全体の重量に対し
31.0重量%のα―リモネンが含有されており、操
作中の香料の蒸発ロスがほとんど無いことが確認
された。 つぎに、この香料組成物323mgを30℃、風速
0.5m/秒の条件下に置き、α―リモネンの放出
量を重量変化と内部標準ガスクロマトグラフイー
で定量分析しながら測定したところ、第3表に示
すとおりの結果を得た。 実施例 8 実施例7で得た素顆粒を使用し、実施例7と同
様の操作でスプレーコーテイングし、素顆粒に対
し65重量%の被膜を形成した。得られた香料組成
物を実施例7と同様に分析したところ、全体の重
量に対し26.0重量%のα―リモネンが含有されて
いた。つぎにこの香料組成物385mgについて実施
例7と同様にα―リモネンの放出量を測定したと
ころ、第3表に示すとおりの結果を得た。 実施例 9 実施例7で得た素顆粒を使用し、この素顆粒に
エチルセルロースのエタノール/トルエン(8/
2重量比)系4%溶液100重量部にタルク1.5重量
部を懸濁した懸濁液を流動装置中で33℃の空気を
流動媒体としてスプレーコーテイングし、素顆粒
に対し50重量%の被膜を形成した。この香料組成
物を実施例7と同様に分析したところ、全体の重
量に対し28.4重量%のα―リモネンが含有されて
いた。つぎに、この香料組成物352mgについて実
施例7と同様にα―リモネンの放出量を測定した
ところ、第3表に示すとおりの結果を得た。
[Table] Example 7 30 parts by weight of soft silicic anhydride was mixed with 30 parts by weight of α-limonene, and then 180 parts by weight of a 5% methylene chloride/ethanol (9/1 weight ratio) solution of cellulose acetate was added as a binder. The mixture was added and kneaded and granulated using a known extrusion granulation device to obtain spherical and cylindrical elementary granules with an average particle diameter of 1 mm. Next, a 4% solution of ethylcellulose in ethanol/toluene (8/2 weight ratio) was added to the elementary granules.
A suspension prepared by suspending 4 parts by weight of talc in 100 parts by weight was spray coated in a fluidizer using air at 36° C. as a fluidizing medium to form a coating of 40% by weight on the elementary granules. During the coating operation, no particle adhesion occurred and a good coating operation was achieved. The obtained fragrance composition is dissolved and extracted in acetone,
When analyzed by gas chromatography using methyl laurate as an internal standard, it was found that
It was confirmed that it contained 31.0% by weight of α-limonene, and that there was almost no evaporation loss of fragrance during operation. Next, 323 mg of this fragrance composition was heated at 30°C and at a wind speed.
When placed under conditions of 0.5 m/sec and quantitatively analyzing the amount of α-limonene released using weight change and internal standard gas chromatography, the results shown in Table 3 were obtained. Example 8 Using the elementary granules obtained in Example 7, spray coating was carried out in the same manner as in Example 7 to form a coating of 65% by weight on the elementary granules. When the obtained fragrance composition was analyzed in the same manner as in Example 7, it was found that it contained 26.0% by weight of α-limonene based on the total weight. Next, the amount of α-limonene released was measured for 385 mg of this perfume composition in the same manner as in Example 7, and the results shown in Table 3 were obtained. Example 9 The elementary granules obtained in Example 7 were used, and ethylcellulose ethanol/toluene (8/
2 weight ratio) A suspension of 1.5 parts by weight of talc in 100 parts by weight of a 4% solution of the system was spray coated in a fluidizer using air at 33°C as a fluidizing medium to form a 50% by weight coating on the elementary granules. Formed. When this perfume composition was analyzed in the same manner as in Example 7, it was found that α-limonene was contained in an amount of 28.4% by weight based on the total weight. Next, the amount of α-limonene released from 352 mg of this fragrance composition was measured in the same manner as in Example 7, and the results shown in Table 3 were obtained.

【表】 第3表の結果より実施例7〜9の場合にもすぐ
れた徐放性を示すことが確認された。 実施例 10 実施例7で得た素顆粒50重量部にヒドロキシプ
ロピルメチルセルロース(信越化学社製商品名
TC―5R)の25%水溶液50重量部を添加しコーテ
イングした後、タルク40重量部を添加して粒状に
保ちつゝ、流動乾燥した。得られた香料組成物を
実施例7と同様に分析したところ、全体の重量の
24.6重量%のα―リモネンが含有されていた。 実施例 11〜13 実施例7〜9に準じ、香料、不活性担体、結合
剤、フイルム形成性重合体および無機質粉末のそ
れぞれ種類および含有量が第4表に示すとおりの
ものである徐放性香料組成物を製造した。これら
はいずれも良好な徐放性を示すものであつた。
[Table] From the results in Table 3, it was confirmed that Examples 7 to 9 also exhibited excellent sustained release properties. Example 10 Hydroxypropyl methylcellulose (trade name manufactured by Shin-Etsu Chemical Co., Ltd.) was added to 50 parts by weight of the elementary granules obtained in Example 7.
After coating by adding 50 parts by weight of a 25% aqueous solution of TC-5R), 40 parts by weight of talc was added to keep it granular and fluidized drying was carried out. When the obtained fragrance composition was analyzed in the same manner as in Example 7, it was found that the total weight of
It contained 24.6% by weight of α-limonene. Examples 11 to 13 Sustained release according to Examples 7 to 9, in which the types and contents of fragrance, inert carrier, binder, film-forming polymer, and inorganic powder are as shown in Table 4. A perfume composition was produced. All of these exhibited good sustained release properties.

【表】【table】

Claims (1)

【特許請求の範囲】 1 香料を吸着した不活性担体粉末を、結合剤に
より造粒してなる固形粒子の全表面を、フイルム
形成性重合体またはこれと無機質粉末との混合物
からなる、香料に対し透過性を有する連続層状の
被膜層で被覆して成り、該香料と不活性担体との
重量比率が1:0.3〜1:10、不活性担体と結合
剤との重量比率が1:0.1〜1:3、フイルム形
成性重合体と無機質粉末との重量比率が1:0〜
1:4である徐放性香料組成物。 2 香料と共に香料安定剤を添加配合してなる特
許請求の範囲第1項記載の徐放性香料組成物。 3 固形粒子が平均粒子径0.3〜10mmの粒状物で
ある特許請求の範囲第1項記載の徐放性香料組成
物。 4 結合剤が香料と相溶する溶媒に溶解するもの
である特許請求の範囲第1項記載の徐放性香料組
成物。 5 結合剤が多糖類および多糖類誘導体よりなる
群から選択される1種または2種以上のものであ
る特許請求の範囲第1項記載の徐放性香料組成
物。 6 フイルム形成性重合体が沸点120℃以下の溶
媒に溶解するものである特許請求の範囲第1項記
載の徐放性香料組成物。 7 フイルム形成性重合体が多糖類および多糖類
誘導体よりなる群から選択される1種または2種
以上のものである特許請求の範囲第1項記載の徐
放性香料組成物。 8 前記多糖類誘導体がセルロース誘導体である
特許請求の範囲第5項または第7項記載の徐放性
香料組成物。 9 香料を吸着した不活性担体粉末を、香料と相
溶する溶媒に溶解した結合剤溶液を用いて造粒し
た後、乾燥して固形粒子となし、これを流動状態
に保持しながら、その全表面にフイルム形成性重
合体の沸点120℃以下の溶媒溶液またはこれの無
機質粉末との混合溶液を噴霧し、乾燥させて、固
形粒子の全表面に香料に対し透過性を有する連続
層状の被膜層を形成させることを特徴とする徐放
性香料組成物の製造方法。 10 香料を吸着した不活性担体粉末を、香料と
相溶する溶媒に溶解した結合剤溶液を用いて造粒
した後、乾燥して固形粒子となし、これにフイル
ム形成性重合体の沸点120℃以下の溶媒溶液を添
加して固形粒子の全表面をコーテイングし、これ
に無機質粉末を加えて粒状に保ち、ついで乾燥さ
せて、固形粒子の全表面に香料に対し透過性を有
する連続層状の被膜層を形成させることを特徴と
する徐放性香料組成物の製造方法。
[Scope of Claims] 1. The entire surface of solid particles obtained by granulating inert carrier powder adsorbed with a fragrance using a binder is coated with a fragrance consisting of a film-forming polymer or a mixture of the same and an inorganic powder. The perfume and the inert carrier are coated with a continuous layer-like coating layer that is permeable to the fragrance, and the weight ratio of the fragrance and the inert carrier is 1:0.3 to 1:10, and the weight ratio of the inert carrier and the binder is 1:0.1 to 1:0.1. 1:3, the weight ratio of film-forming polymer and inorganic powder is 1:0 to
A sustained release fragrance composition with a ratio of 1:4. 2. The sustained-release fragrance composition according to claim 1, which comprises a fragrance stabilizer and a fragrance. 3. The sustained release fragrance composition according to claim 1, wherein the solid particles are granules having an average particle diameter of 0.3 to 10 mm. 4. The sustained release fragrance composition according to claim 1, wherein the binder is dissolved in a solvent that is compatible with the fragrance. 5. The sustained release fragrance composition according to claim 1, wherein the binder is one or more selected from the group consisting of polysaccharides and polysaccharide derivatives. 6. The sustained release fragrance composition according to claim 1, wherein the film-forming polymer is soluble in a solvent having a boiling point of 120°C or lower. 7. The sustained release fragrance composition according to claim 1, wherein the film-forming polymer is one or more selected from the group consisting of polysaccharides and polysaccharide derivatives. 8. The sustained release fragrance composition according to claim 5 or 7, wherein the polysaccharide derivative is a cellulose derivative. 9 The inert carrier powder adsorbing the fragrance is granulated using a binder solution dissolved in a solvent that is compatible with the fragrance, and then dried to form solid particles. A solvent solution of a film-forming polymer with a boiling point of 120°C or less or a mixed solution of this with an inorganic powder is sprayed onto the surface and dried to form a continuous layered coating layer that is permeable to perfume over the entire surface of the solid particles. 1. A method for producing a sustained-release fragrance composition, the method comprising: forming a sustained-release fragrance composition. 10 The inert carrier powder adsorbing the fragrance is granulated using a binder solution dissolved in a solvent compatible with the fragrance, and then dried to form solid particles, which are then granulated with the boiling point of the film-forming polymer at 120°C. The following solvent solution is added to coat the entire surface of the solid particles, an inorganic powder is added to this to maintain the granular shape, and the solid particles are then dried to form a continuous layered coating that is permeable to perfume on the entire surface of the solid particles. A method for producing a sustained release fragrance composition, which comprises forming a layer.
JP58124161A 1983-06-20 1983-07-08 Slow-releasing perfumery composition and its preparation Granted JPS6016914A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP58124161A JPS6016914A (en) 1983-07-08 1983-07-08 Slow-releasing perfumery composition and its preparation
CA000456814A CA1244343A (en) 1983-06-20 1984-06-18 Sustainedly vapor-releasing body for environmental control
AU29471/84A AU566939B2 (en) 1983-06-20 1984-06-18 A sustainedly vapor releasing body for environment control
EP19840107132 EP0131783B1 (en) 1983-06-20 1984-06-20 A sustainedly vapor-releasing body for environmental control
BR8403042A BR8403042A (en) 1983-06-20 1984-06-20 CONTINUOUS STEAM RELEASING BODY
DE8484107132T DE3479698D1 (en) 1983-06-20 1984-06-20 A sustainedly vapor-releasing body for environmental control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58124161A JPS6016914A (en) 1983-07-08 1983-07-08 Slow-releasing perfumery composition and its preparation

Publications (2)

Publication Number Publication Date
JPS6016914A JPS6016914A (en) 1985-01-28
JPS6229056B2 true JPS6229056B2 (en) 1987-06-24

Family

ID=14878447

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58124161A Granted JPS6016914A (en) 1983-06-20 1983-07-08 Slow-releasing perfumery composition and its preparation

Country Status (1)

Country Link
JP (1) JPS6016914A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0250051A (en) * 1988-08-08 1990-02-20 Sanyo Electric Co Ltd Outdoor unit of separate type air conditioner

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RS61105B1 (en) * 2014-06-06 2020-12-31 Opes Corp Oy Mass containing functional compound and viscosity regulator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5849151A (en) * 1981-09-18 1983-03-23 日東電工株式会社 Granular aroma release material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0250051A (en) * 1988-08-08 1990-02-20 Sanyo Electric Co Ltd Outdoor unit of separate type air conditioner

Also Published As

Publication number Publication date
JPS6016914A (en) 1985-01-28

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