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JPH0563184B2 - - Google Patents
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JPH0563184B2 - - Google Patents

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Publication number
JPH0563184B2
JPH0563184B2 JP60175758A JP17575885A JPH0563184B2 JP H0563184 B2 JPH0563184 B2 JP H0563184B2 JP 60175758 A JP60175758 A JP 60175758A JP 17575885 A JP17575885 A JP 17575885A JP H0563184 B2 JPH0563184 B2 JP H0563184B2
Authority
JP
Japan
Prior art keywords
fragrance
gel
transparent
volatilization
sbc
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 - Fee Related
Application number
JP60175758A
Other languages
Japanese (ja)
Other versions
JPS6238166A (en
Inventor
Juichi Matsumoto
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.)
Soda Aromatic Co Ltd
Original Assignee
Soda Aromatic 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 Soda Aromatic Co Ltd filed Critical Soda Aromatic Co Ltd
Priority to JP60175758A priority Critical patent/JPS6238166A/en
Publication of JPS6238166A publication Critical patent/JPS6238166A/en
Publication of JPH0563184B2 publication Critical patent/JPH0563184B2/ja
Granted legal-status Critical Current

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は芳香剤として使用する透明ゲル状の香
料揮散体及びその製造法に関する。 (従来の技術) 従来から、芳香剤としては種々のタイプのもの
が実用されている。 本発明者は先にエチレン・醋酸ビニールコポリ
マーの粒状ペレツトに香料を含浸吸収せしめて成
る粒状の香料揮散体を提案した(特公昭60−2064
号)。この香料揮散体はその優れた徐放効果等か
ら今日広く実用されている。このような粒状の香
料揮散体の例としては他にも特公昭59−27784号
等が知られている。 これらの粒状の香料揮散体は製造が容易であ
り、また香料を粒状の樹脂に含浸吸収させるた
め、香料を含有させた樹脂を高温下で斜出成形し
て得るタイプの香料揮散体に比し、製造過程での
香料の劣化や揮散損失等がないという利点を有す
るが、それを芳香剤として商品形態にするために
は粒状なるが故に必ず粒径以下のスリツトを設け
た全密封型の容器を用いざるを得ず従つて折角美
麗な色に着色しても、ユーザーの目には触れにく
いという欠点を有し、且つ何にもまして不利な点
は揮散終了のエンドポイントが視覚により判定出
来ないことである。これは香料の揮散による粒状
物の見掛け体積の減少がごくわずかであることに
原因している。揮散終了のエンドポイントが視覚
により容易に判定出来るタイプの香料揮散体の一
つとして液状の香料揮散体がある。これは内容物
の量を透視可能な容器に入れて用い、内容物の減
少から容易に揮散終了のエンドポイントを判定で
きる。しかし液状の香料揮散体は液状なるが故に
使用時外力によつて流出しやすい等保管性に問題
がありまた容器の工夫により保管性を高めようと
すると揮散量の維持が困難になる等の問題が派生
する。 このような欠点を持たず且つ揮散終了のエンド
ポイントを容易に判定出来るものとしてゲル状香
料揮散体がある。その代表例としてカラギーナン
をゲル化剤とし水を溶媒として、これに適宜な量
の調合香料と乳化用の界面活性剤を加えて成る、
所謂水性ゲルがある。かかる水性ゲルは、通常2
〜3重量%のカラギーナン粉末を水中に分散さ
せ、100℃前後までの加熱攪拌を加えて完全な溶
液とし、一旦55℃〜60℃前後まで冷やしてから
(香料の熱劣化を避ける為)5〜8重量%の調合
香料と1重量%前後の乳化用界面活性剤との混合
液を加えて攪拌乳化せしめた上で、適宜な容器に
注入して冷却し容器なりの形状にゲル状に固化せ
しめるといつた製造法で作られる。溶媒が沸点
100℃の水であるので香料を伴つての揮散速度が
早く、且つ揮散の進行に伴いゲルの体積が収縮し
その終期には始めの体積の1/10以下にまで収縮乾
固するので、揮散終了のエンドポイントを容易に
視認出来るという大きな利点を持つている。十数
年の商品寿命を保ち、今なお芳香剤の主流の座を
占めている所以もここにある。 然しその反面、この水ゲルは次のような欠点も
有している。 a 界面活性剤の使用を必須とする乳化型なので
その外観は著しく不透明であり、従つて種々の
色調に着色されても必ずしも美麗とは言い難
い。 b 揮散が早すぎて、通気孔や露出面積の調節に
よる揮散調整が難かしく、その調整宜しきを得
ない場合は1週間〜10日前後の間に収縮乾固し
てしまうことが多い。 c ゲルの弾性が小さいので外力により損壊しや
すい。 (発明が解決しようとする問題点) 本発明は従来のカラギーナン系水性ゲルの利点
即ち収縮乾固してエンドポイントを示すという性
質はそのまま保有し、その欠点を無くした、透明
で(美麗な外観)弾性に富み(外力に強い)且つ
適当な揮散期間を有する新規ゲル状香料揮散体を
提供することを目的とするものである。 (問題点解決するための手段) 本発明のゲル状香料揮散体は、液状脂肪族炭化
水素をスチレン系熱可塑性エラストマーでゲル化
してなる透明ゲル状物とその中に含有させた香料
とからなるものである。 本発明のゲル状香料揮散体は、ゲル化剤として
のスチレン系熱可塑性エラストマー(Stylene
Blo−ck Co−polimer、以下略してSBCと略記
する)と、被ゲル化溶媒としての無臭乃至は微臭
の液状脂肪族炭化水素とから得られる透明ゲル状
物を用いる点に特徴を有する。 本発明にゲル化剤として使用するSBCは、常
温下では加硫ゴムの、高温下では普通の熱可塑性
樹脂の特性を示す熱可塑性エラストマーの一種で
あり、ハードセグメント(硬質相)にポリスチレ
ンブロツク、ソフトセグメント(軟質相)にゴム
ブロツクを持ち、ポリスチレン部分が物理架橋
(ドメイン)を形成して橋かけ点になつているブ
ロツクコポリマーである。現在、ゴムブロツクが
ポリブタジエンであるスチレン・ブタジエン・ス
チレンブロツクコポリマー(S−B−Sと略記さ
れる。以下この略記を用いる)、ゴムブロツクが
ポリイソプレンであるスチレン・イソプレン・ス
チレンブロツクコポリマー(S−I−Sと略記さ
れる。以下この略記を用いる)、ゴムブロツクが
ポリオレフイン(エチレン、ブチレン)であるス
チレン・エチレン・ブチレン・ブチレンブロツク
コポリマー(S−E・B−Sと略記される。以下
この略記を用いる)の三種が主として上市されて
いる。その主たる用途は一般成型材料、プラスチ
ツク改質材、粘、接着剤のベースポリマー等であ
る。形態は殆どがペレツト状かクラム(パン屑)
状であるが、粉末状のものもある。 本発明のゲル化剤としてはSBCであれば本質
的にはいずれの使用も可能であり、S−E・B−
S,S−B−S,S−I−Sのいずれも好ましく
使用される。いずれも透明なゲルを与えるが、ゴ
ムブロツクによつて生成ゲルの透明度に僅か乍ら
差があり、強いて順位をつけるならば、S−E・
B−Sが完全透明であり、S−B−Sがこれに次
ぎ、S−I−Sが若干落ちる傾向にある。SBC
の使用量と生成ゲルの強度は使用するSBCのポ
リスチレン含量(通常スチレン/ゴム比で表わさ
れる)及び分子量により左右される。使用量を一
定にした場合ポリスチレン含量が小さい程、そし
て分子量が小さい程、生成ゲルの強度は弱くなる
傾向にある。経済性を加味した使用量で、通常の
カラギーナン系水性ゲルと同等か、それ以上の強
度のゲルを得る為のSBCのポリスチレン含量及
び分子量はスチレン/ゴム比30/70以上、分子量
100000以上であることが望ましく、スチレン/ゴ
ム比35/65、分子量200000以上であることがより
一層望ましい。 又本発明に被ゲル化溶媒として使用する液状脂
肪族炭化水素は無臭乃至は使用する香料の香調を
阻害しない程度の微臭のものであれば何でもよい
が、100℃より高い沸点を有するもの、好ましく
は沸点150℃〜300℃の範囲、より好ましくは150
℃〜250℃の範囲の、ノルマルパラフイン、イソ
パラフイン等が望ましい。一般には石油系炭化水
素溶媒として上市されている飽和脂肪族炭化水素
を主成分とする混合溶媒が好ましく用いられる。
所望のゲル状物を形成し得る範囲で芳香族炭化水
素等の他の溶媒も併用しうる。 本発明のゲル状香料揮散体は、 (イ) (a)SBC(ペレツト状、クラム状、粉末状を問
わず)を液状脂肪族炭化水素(以下OAHCと
記載する)に加えて加熱攪拌により粘稠な透明
溶融液とし、そこで、所定量の香料を加えて均
一透明に溶解させた後、室温まで冷却するか、
又は(b)SBCとOAHCの粘稠な透明溶融液を室
温まで冷却して一旦透明ゲルと為し、これに香
料を接触により吸収せしめるか、若しくは(c)予
め所定量の香料をOAHCに溶解させて置き、
この香料入OAHCにSBCを加えて加熱攪拌に
より粘稠な透明溶融液とし、これを室温まで冷
却して透明ゲル状香料揮散体とするいずれかの
方法(加熱溶融法)或いは (ロ) 予め所定量の香料を溶解せしめたOAHCに
SBCの粉末を分散させ、(イ)の方法に要した温
度より遥かに低い、香料を熱劣化せしめない範
囲の温度下に短時間静置して透明ゲル状揮散体
とする方法(粉末分散膨潤法)等 により製造することが出来る。(イ)の(a)法はカラギ
ーナン等の水性ゲルの製造に多用される方法で最
も簡便な製法といえる。 然し乍ら、SBCは後述する如く、ドメイン
(物理架橋)を形成するポリスチレンのガラス転
移点が約90℃と高いので(イ)の加熱溶融法に於て
SBCをOAHCに溶融せしむる為には相当な高温
を要する。SBCの使用量が少ない時、例えば5
重量%以下の様な場合には辛うじて100℃以下の
温度で溶融せしめることが可能であるが、その使
用量が多い時例えば10重量%前後の場合には120
℃〜150℃位の高温を必要とする。従つて、前者
の場合には(イ)の(a)及び(c)の製法が辛うじて可能と
なるが、後者の場合には、香料の熱劣化を避け難
いので(イ)の(b)法に依らざるを得ず、香料の接触吸
収の為の24〜72時間の時間ロスを忍ばざるを得な
い。 (ロ)の粉末分散膨潤法は、かかる製造上の不便さ
を解消する為に考案されたより有利な製造法であ
る。 この方法はSBCの粉末を用いて実施した(イ)の
加熱溶融法の(a)及び(c)の過程中に生ずる現象、−
−−SBC粉末を分散せしめたOAHC、及び同じ
くSBC粉末を分散せしめた香料入のOAHCはい
ずれもSBCの完全溶融に要する温度の約1/2位の
温度に達した時点でSBC粉末を含んだ白濁状態
のまま一旦急激にゲル化してしまい、攪拌プロペ
ラや攪拌バーを止めてしまう。この後更に加温を
続けると、昇温に伴いこの白濁ゲルが徐々に加熱
面に近い部分から透明に溶融し始め、完全溶融に
至る−−−をヒントに確立したものである。本発
明者は上述の白濁ゲル化の時点で昇温を中止し、
それ以降、白濁ゲル化時の温度を保持させてみた
ところ白濁ゲルは徐々に透明化して行き、最後に
は完全な透明溶融液を冷却して出来た透明ゲルと
全く同一の透明ゲルとなつたのである。即ちこの
製造法によるならば例えば10重量%のSBC粉末
を用い加熱溶融法で140℃を要する場合でも、そ
の1/2の70℃で透明ゲル化が可能になるわけであ
り、従つて香料の熱劣化を懸念することなしに、
所定量のSBC粉末と、予め香料を溶解せしめた
所定量のOAHCを仕込んだ商品容器を所要温度
の空気浴中で一定時間加温するという簡易な方法
で、透明な、弾性に富むゲル状香料揮散体を母体
とした芳香剤商品が製造出来るのである。尚、加
温前に減圧による脱泡処理をした方がより美麗な
ゲルが得られることは言うまでもない。 使用するSBCの形態は加熱溶融法の場合はペ
レツト状クラム状で差支えはないが溶融時間を短
縮する為には粉末状が望ましい。分散膨潤法の場
合はゲル化のメカニズムから粉末状のものを用い
る必要がある。 分散膨潤法に於ける透明ゲル化のメカニズムは
発明者の実験及び観察によれば(1)SBC粉体粒子
のOAHCの吸収による膨潤、(2)飽和膨潤粒子相
互の融着による不透明ゲル化、(3)透明化といつた
経過をたどるものと思われる。 本発明に使用する香料は被ゲル化溶媒である
OAHCに透明に溶解することが必須条件となる
が、通常の調合香料は炭化水素、エステル、エー
テル等の如く炭化水素に易溶の成分を充分に含有
しているので、殆ど問題はない。また香料と共に
防虫剤や難燃剤その他の適宜の成分を併用するこ
ともできる。 かくして得られる本発明の透明ゲル状香料揮散
体の各成分の含有量はそれぞれの組合せに応じ最
適量を異にするが、通常SBC5〜25重量%、香料
3〜10重量%、OAHC92〜65重量%である。 透明ゲルへの着色は、必要に応じ、目的とする
色調の油溶性染料を、使用する香、若しくは
OAHCに予め溶解せしめて置くことで容易に達
せられる。 (発明の効果) 本発明の効果を列挙すれば下記の通りである。 a カラギーナン系水性ゲル状香料揮散体の持つ
最大の利点、即ち、揮散に伴い収縮乾固して揮
散終了のエンドポイントを示すという特性はそ
のまま残されている。 b その外観は美麗な透明性であり、且つその透
明性は揮散の終期まで保持される。 c ゲルは極めて弾性に富み外力に対して強い。 d 揮散性向は理想的な徐放型であり、従つて揮
散の調節がカラギーナン系より容易である。 (実施例) 以下実施例により、より詳細に、より具体的に
説明するが、本発明はこれによつて限定されるも
のではない。 実施例 1 市販の円錐切断型の摺動上下式の蓋のついた水
性ゲル芳香剤の空容器(仕込容量160c.c.)にスチ
レン系熱可塑性エラストマーとしてシエル化学製
のS−E・B−S商品名クレートンG−1651の粉
末(16メツシユ以下)13.2g(12部)を充填し、こ
れに初溜174℃、乾点207℃のイソパラフイン(シ
エル化学製、商品名Shellsol 71)88g(80部)と
油溶性染料でオレンジ色に着色したキンモクセイ
系調合香料8.8g(8部)との混合溶液を注入し、
水銀柱100mmで脱泡した後密栓し、100に調整され
た恒温槽内に35分間静置して加温(昇温測定用の
サンプルによる測定結果では35分目の内容物温度
は73℃であつた)し、室温までの冷却を待つて蓋
をとると、オレンジ色の完全透明な弾性に富んだ
芳香ゲル体に仕上がつていた。この容器入芳香ゲ
ル体につき、容器倒立の条件下での50℃及び−10
℃下24時間の虐待試験を実施したが高温によるゲ
ルの流動や変型、低温による離液現象等は全くみ
られなかつた。又、蓋半開、容積約4m3の水洗ト
イレ内定置、平均気温15℃、日数60日間の揮散及
び官能試験も実施したが、期間内香気強度4.0〜
2.75(6段階臭気強度表示法による数値、以下、
単に数値のみで表現する。註1参照)、揮散率
(揮散量/可揮散成分総量、以下、単に揮散率と
略記する。)94%と極めて良好な結果が得られた。
そして揮散終了したゲル残渣は色調は濃くなつた
がその美麗な透明性をなお保持していた。 比較の為、本例に使用した容器に流し込み、冷
却してゲル化したカラギーナン系水性ゲル状香料
揮散体(カラギーナン粉末2.2g、海面活性剤1.1g
キンモクセイ系調合香料8.8g、水97.9g計110g)
につき前述のSBCゲルの場合と全く同条件下で
揮散及び官能試験を実施したが30日間で早くも揮
散率96%に達し、完全に収縮乾固の外観となつて
しまい、期間内の香気強度は4.25〜2.75であつ
た。 実施例 2 適宜な容器にシエル化学製のS−E・B−S商
品名クレートンG−1651 10部を採り、これに初
溜174℃、乾点207℃のイソパラフイン(シエル化
学製、商品名Shellsol 71)90部を加え加熱攪拌
しつつ溶融せしめて行き、140℃で完全透明な高
粘度溶液となつたところで、これを直径75mm、深
さ23mm、容量100c.c.のプルトツプ罐に65g注入し、
室温で徐冷して完全透明なゲル体となるのを待
ち、これにオレンジ色の油溶性染料でオレンジ色
に着色したキンモクセイ系調合香料5gを加え、
巻締機で罐底を閉じた。この充填済密封罐を室温
下に72時間放置した後、プルトツプ面から開罐し
てみると香料はゲル体に、手指で触れても指が全
く濡れない状態にまで完全に含浸吸収され、オレ
ンジ色の完全透明な弾性に富んだ芳香ゲル体に仕
上がつていた。この開封罐入芳香ゲル体につき容
積約4m3の水洗トイレ内定置、平均気温15℃、日
数60日間の揮散及び官能試験を実施したが期間内
の香気強度は3.5〜2.5、揮散率78%という結果が
得られ、罐内に残つた収縮ゲル体は、未だ10〜20
日間の香気揮散が可能な状態であり、なお元の美
麗な透明性を保持していた。 実施例 3 実施例−1に使用した芳香剤空容器にシエル化
学製のS−B−S(商品名カリフレツクスTR−
1184、スチレン/ゴム比30/70、分子量150000)
の粉末(16メツシユ以下)22g(20部)を充填し、
これに初溜174℃、乾点207℃のイソパラフイン
(シエル化学製商品名Shellsol 71)79.2g(72部)
と、予め緑色系油溶性染料で淡緑色に着色した、
青リンゴ系の調合香料8.8g(8部)との混合溶液
88g(80部)を注入し、水銀柱100mmで脱泡後密栓
し、70℃の調整された恒温槽内に45分間静置して
加温(45分目の内容物温度は68℃)し、室温まで
の冷却を待つて蓋をとると、淡緑色の殆ど透明な
弾性に富んだ芳香ゲル体に仕上がつていた。この
容器入芳香ゲル体につき、容器倒立の条件下での
50℃及び−10℃下24時間の虐待試験を実施したが
高温によるゲルの流動や変型、低温による離液現
象等は全くみられなかつた。又、蓋半開、容積約
4m3の水洗トイレ内定置、平均気温15℃、日数60
日間の揮散及び官能試験を実施したが、期間内香
気強度4.0〜2.75、揮散率92%と極めて良好な結
果が得られた。そして揮散終了したゲル体残渣は
色調は濃くなつたが元の透明性をなお保持してい
た。 実施例 4 適宜な容器にシエル化学製のS−I−S(商品
名カリフレツクスTR−1111、スチレン/ゴム比
21/79、分子量100000)25部を採り、これに初溜
174℃、乾点207℃のイソパラフイン(シエル化学
製、商品名Shellsol 71)75部を加え、加熱攪拌
しつつ溶融せしめて行き、130℃で殆ど透明な高
粘度溶液となつたところで、これを直径75mm、深
さ23mm、容量100c.c.のプルトツプ罐に65g注入し、
室温で徐冷して殆ど透明な弾性に富むゲル体にな
るのを待ち、これに黄色系油溶性染料で黄色に着
色したレモン系調合香料5gを加え、巻締機で罐
底を閉じた。この充填済密封罐を室温下に72時間
放置した後、プルトツプ面から開罐してみると香
料はゲル体に、手指で触れても指が全く濡れない
状態にまで完全に含浸吸収され、淡黄色の殆ど透
明な弾性に富んだ芳香ゲル体に仕上がつていた。
この開封罐入芳香ゲル体につき、容積約4m3の水
洗トイレ内定置、平均気温15℃、日数60日間の揮
散及び官能試験を実施したが、期間内の香気強度
は3.5〜2.5、揮散率76%という結果が得られ、罐
内に残つた収縮ゲル体は、未だ10〜20日間位の香
気揮散が可能な状態であり、なお元の透明性を保
持していた。 実施例 5 適宜な容器にシエル化学製のS−E・B−S商
品名クレートンG−1651の粉末4部を採り、これ
に初溜174℃、乾点207℃のイソパラフイン(シエ
ル化学製、商品名Shellsol 71)86部と、予めオ
レンジ系油溶性染料でオレンジ色に着色したキン
モクセイ系の調合香料10部との混合液を加え、加
熱攪拌しつつ、溶融せしめて行くと85℃で透明な
高粘度溶液となつた。これを直径75mm、深さ23mm
容量100c.c.のプルトツプ罐に65g注入し、室温で
徐冷すると、強度はやや落ちるが、オレンジ色の
完全透明な弾性に富んだ芳香ゲル体となつた。こ
の状態で容積約4m3の水洗トイレ内定置、平均気
温15℃、日数60日間の揮散及び官能試験を実施し
たが、揮散率は96%、期間内香気強度3.5〜2.75
という結果が得られた。そして揮散終了したゲル
体残渣はなお元の透明性を保持していた。 【表】
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a transparent gel-like fragrance volatile material used as an aromatic agent and a method for producing the same. (Prior Art) Various types of fragrances have been used in practice. The present inventor previously proposed a granular fragrance volatile material made by impregnating and absorbing a fragrance into granular pellets of ethylene/vinyl acetate copolymer (Japanese Patent Publication No. 60-2064).
issue). This perfume volatilizer is widely used today due to its excellent sustained release effect. Japanese Patent Publication No. 59-27784 is also known as an example of such a granular perfume volatile material. These granular fragrance volatile materials are easy to manufacture, and because the fragrance is impregnated and absorbed into granular resin, they are more expensive than the type of fragrance volatile material obtained by extrusion molding resin containing fragrance at high temperatures. It has the advantage that there is no deterioration or volatilization loss of the fragrance during the manufacturing process, but in order to make it into a product as a fragrance, it must be in a completely sealed container with a slit smaller than the particle size because it is granular. Therefore, even if it is colored in a beautiful color, it has the disadvantage that it is difficult for the user to see, and the most disadvantageous point is that the end point of the end of volatilization cannot be determined visually. There is no such thing. This is due to the fact that the apparent volume of the granules decreases only slightly due to volatilization of the fragrance. A liquid fragrance volatilizer is one type of perfume volatilizer whose end point of volatilization can be easily determined visually. This is used by placing the amount of the contents in a container that can be seen through, and the end point of volatilization completion can be easily determined from the decrease in the contents. However, because the liquid flavor volatilizer is in a liquid state, there are problems with storage, such as the fact that it tends to flow out due to external force during use, and if storage is attempted to be improved by devising a container, it becomes difficult to maintain the amount of volatilization. is derived. There is a gel-like fragrance volatilization material that does not have such drawbacks and can easily determine the end point of completion of volatilization. A typical example is carrageenan as a gelling agent, water as a solvent, and an appropriate amount of blended fragrance and emulsifying surfactant added thereto.
There is a so-called aqueous gel. Such aqueous gels usually contain 2
~3% by weight of carrageenan powder is dispersed in water, heated and stirred to around 100°C to make a complete solution, and once cooled to around 55°C to 60°C (to avoid thermal deterioration of the fragrance), 5~ A mixture of 8% by weight of blended fragrance and about 1% by weight of emulsifying surfactant is added, stirred and emulsified, poured into an appropriate container, cooled and solidified into a gel-like shape in the shape of the container. It is made using the same manufacturing method. the boiling point of the solvent
Since the water is at 100℃, the rate of volatilization along with the fragrance is fast, and as the volatilization progresses, the volume of the gel shrinks and dries to less than 1/10 of its initial volume, so it is difficult to volatilize. It has the great advantage of being able to easily see the termination endpoint. This is the reason why it has maintained a product lifespan of more than ten years and is still the mainstream of air fresheners. However, on the other hand, this water gel also has the following drawbacks. a) Since it is an emulsion type that requires the use of a surfactant, its appearance is extremely opaque, and therefore it cannot necessarily be said that it is beautiful even if it is colored in various tones. b. The volatilization rate is too fast, making it difficult to adjust the volatilization by adjusting the ventilation holes or exposed area. If the volatilization cannot be adjusted properly, it often shrinks to dryness within a week to 10 days. c Because the gel has low elasticity, it is easily damaged by external force. (Problems to be Solved by the Invention) The present invention retains the advantages of conventional carrageenan-based aqueous gels, that is, the property of shrinking and drying to show an end point, but eliminates the disadvantages, and has a transparent (beautiful appearance) gel. ) The object of the present invention is to provide a novel gel-like fragrance volatilization material that is highly elastic (resistant to external forces) and has an appropriate volatilization period. (Means for Solving the Problems) The gel-like fragrance volatile material of the present invention consists of a transparent gel-like substance formed by gelling a liquid aliphatic hydrocarbon with a styrene-based thermoplastic elastomer, and a fragrance contained therein. It is something. The gel-like fragrance volatile material of the present invention uses a styrene thermoplastic elastomer (Stylene) as a gelling agent.
It is characterized in that it uses a transparent gel-like material obtained from Block Co-polymer (hereinafter abbreviated as SBC) and an odorless or slightly odorless liquid aliphatic hydrocarbon as a gelling solvent. SBC used as a gelling agent in the present invention is a type of thermoplastic elastomer that exhibits the properties of vulcanized rubber at room temperature and that of ordinary thermoplastic resin at high temperatures, and has polystyrene blocks in the hard segment (hard phase). It is a block copolymer that has rubber blocks in the soft segment (soft phase), and polystyrene portions form physical crosslinks (domains) and serve as crosslinking points. Currently, there are styrene-butadiene-styrene block copolymers (abbreviated as S-B-S, hereinafter used) whose rubber blocks are polybutadiene, and styrene-isoprene-styrene block copolymers (S-I-S) whose rubber blocks are polyisoprene. A styrene-ethylene-butylene-butylene block copolymer whose rubber blocks are polyolefins (ethylene, butylene) (abbreviated as S-E-B-S, hereinafter this abbreviation will be used). ) are mainly on the market. Its main uses include general molding materials, plastic modifiers, and base polymers for adhesives and adhesives. The form is mostly pellet-like or crumbs (bread crumbs)
There is also a powder form. As the gelling agent of the present invention, essentially any SBC can be used, and S-E, B-
S, S-B-S, and S-I-S are all preferably used. All of them give a transparent gel, but there is a slight difference in the transparency of the gel produced depending on the rubber block.
B-S is completely transparent, followed by S-B-S, and S-I-S tends to be slightly transparent. SBC
The amount used and the strength of the resulting gel depend on the polystyrene content (usually expressed as the styrene/rubber ratio) and molecular weight of the SBC used. When the amount used is constant, the lower the polystyrene content and the lower the molecular weight, the weaker the strength of the resulting gel tends to be. The polystyrene content and molecular weight of SBC should be styrene/rubber ratio of 30/70 or more and molecular weight to obtain a gel with the same or higher strength than ordinary carrageenan-based aqueous gels at an economical usage amount.
It is desirable that the molecular weight be 100,000 or more, and it is even more desirable that the styrene/rubber ratio be 35/65 and the molecular weight be 200,000 or more. The liquid aliphatic hydrocarbon used as a gelling solvent in the present invention may be of any kind as long as it is odorless or has a slight odor that does not interfere with the fragrance tone of the fragrance used, but it may have a boiling point higher than 100°C. , preferably a boiling point in the range of 150°C to 300°C, more preferably 150°C
Normal paraffin, isoparaffin, etc. in the range of ℃ to 250℃ are preferable. In general, mixed solvents containing saturated aliphatic hydrocarbons as main components, which are commercially available as petroleum-based hydrocarbon solvents, are preferably used.
Other solvents such as aromatic hydrocarbons may also be used in combination as long as the desired gel can be formed. The gel-like fragrance volatile material of the present invention can be obtained by adding (a) SBC (regardless of pellet, crumb, or powder form) to liquid aliphatic hydrocarbon (hereinafter referred to as OAHC) and heating and stirring to make it viscous. Create a viscous transparent melt, add a predetermined amount of fragrance, dissolve uniformly and transparently, and then cool to room temperature.
or (b) cooling a viscous transparent melt of SBC and OAHC to room temperature to form a transparent gel, and allowing the fragrance to be absorbed by contact with this, or (c) dissolving a predetermined amount of fragrance in OAHC in advance. leave it alone,
SBC is added to this fragrance-containing OAHC and heated and stirred to form a viscous transparent melt, which is then cooled to room temperature to form a transparent gel-like fragrance volatile material (heat melting method) or (b) prepared in advance. OAHC in which a fixed amount of fragrance is dissolved
A method of dispersing SBC powder and leaving it for a short period of time at a temperature far lower than that required for method (a), within a range that does not cause thermal deterioration of the fragrance, to form a transparent gel-like volatile material (powder dispersion swelling) It can be manufactured by the following methods. Method (a) of (b) is often used in the production of aqueous gels such as carrageenan, and can be said to be the simplest production method. However, as will be explained later in SBC, the glass transition point of the polystyrene that forms the domains (physical crosslinks) is as high as approximately 90°C.
Considerable high temperatures are required to melt SBC into OAHC. When SBC usage is low, for example 5
If the amount is less than 100℃, it is possible to melt it at a temperature below 100℃, but if the amount used is large, for example, around 10% by weight, it is possible to melt at a temperature of 120℃ or less.
Requires high temperatures of around 150°C. Therefore, in the former case, the production methods in (a) and (c) of (a) are barely possible, but in the latter case, it is difficult to avoid thermal deterioration of the fragrance, so the method (b) of (b) is possible. However, they have no choice but to endure a loss of 24 to 72 hours for contact and absorption of the fragrance. The powder dispersion and swelling method (b) is a more advantageous manufacturing method devised to eliminate such manufacturing inconveniences. This method is based on the phenomena that occur during the steps (a) and (c) of the heating melting method (a) carried out using SBC powder.
--Both OAHC with SBC powder dispersed and fragrance-containing OAHC with SBC powder dispersed contained SBC powder when the temperature reached about 1/2 of the temperature required for complete melting of SBC. Once the liquid is cloudy, it quickly turns into a gel, causing the stirring propeller and stirring bar to stop. After this, when heating is continued, this cloudy gel gradually begins to melt transparently from a portion close to the heating surface as the temperature rises, leading to complete melting. The present inventor stopped the temperature increase at the time of the above-mentioned cloudy gelation,
After that, when we tried to maintain the temperature at which the cloudy gel formed, the cloudy gel gradually became transparent, and in the end it became a transparent gel that was exactly the same as the transparent gel that was created by cooling a completely transparent molten liquid. It is. In other words, with this production method, for example, even if 10% by weight SBC powder is heated at 140°C using the heating melting method, it is possible to form a transparent gel at 70°C, which is half of the temperature required, and therefore the fragrance can be made into a transparent gel. without worrying about thermal deterioration.
A transparent, highly elastic gel-like fragrance can be produced by simply heating a product container containing a specified amount of SBC powder and a specified amount of OAHC in which the fragrance has been dissolved in an air bath at the required temperature for a certain period of time. It is possible to manufacture fragrance products using volatile substances as a base material. It goes without saying that a more beautiful gel can be obtained by defoaming by reducing pressure before heating. The form of SBC to be used may be pellets or crumbs in the case of the heat melting method, but it is preferable to use powder form in order to shorten the melting time. In the case of the dispersion swelling method, it is necessary to use powdered material due to the gelation mechanism. According to the inventor's experiments and observations, the mechanism of transparent gelation in the dispersion swelling method is (1) swelling due to absorption of OAHC by SBC powder particles, (2) opaque gelation due to mutual fusion of saturated swollen particles. (3) It seems to follow the same process as transparency. The fragrance used in the present invention is a gelling solvent.
Transparent dissolution in OAHC is an essential condition, but there is almost no problem since ordinary blended fragrances contain sufficient components that are easily soluble in hydrocarbons, such as hydrocarbons, esters, and ethers. In addition, insect repellents, flame retardants, and other appropriate ingredients can also be used together with fragrances. The optimal content of each component in the transparent gel-like fragrance volatile material of the present invention thus obtained varies depending on the respective combination, but is usually 5 to 25% by weight of SBC, 3 to 10% by weight of fragrance, and 92 to 65% by weight of OAHC. %. To color the transparent gel, use an oil-soluble dye of the desired color, incense, or
This can be easily achieved by pre-dissolving it in OAHC. (Effects of the Invention) The effects of the present invention are listed below. a The greatest advantage of the carrageenan-based aqueous gel fragrance volatile material, that is, the characteristic that it shrinks and dries up as it evaporates, indicating the end point of the end of evaporation, remains intact. b The appearance is beautiful and transparent, and the transparency is maintained until the end of volatilization. c Gel is extremely elastic and strong against external forces. d The volatilization tendency is an ideal sustained release type, and therefore volatilization can be controlled more easily than carrageenan. (Example) The present invention will be described in more detail and more specifically with reference to Examples, but the present invention is not limited thereto. Example 1 A commercially available empty container (capacity: 160 c.c.) of an aqueous gel air freshener with a cone-cut type sliding top and bottom lid was filled with S-E/B- manufactured by Ciel Chemical as a styrene thermoplastic elastomer. Filled with 13.2 g (12 parts) of Kraton G-1651 powder (16 mesh or less) and 88 g of isoparaffin (Shell Chemical Co., Ltd., trade name Shellsol 71) with an initial distillation temperature of 174°C and a dry point of 207°C ( Inject a mixed solution of 80 parts) and 8.8 g (8 parts) of an osmanthus-based blended fragrance colored orange with an oil-soluble dye.
After defoaming with 100 mm of mercury, seal the cap and leave it in a constant temperature bath adjusted to 100 for 35 minutes to heat it (according to the measurement result of the sample for temperature rise measurement, the content temperature at the 35th minute was 73℃. After waiting for it to cool to room temperature, I removed the lid and found that it had finished as an orange, completely transparent, highly elastic, aromatic gel. This aromatic gel body in a container was tested at 50℃ and -10℃ under the condition of upside down container.
A 24-hour abuse test at ℃ was conducted, but no gel flow or deformation caused by high temperatures or syneresis caused by low temperatures were observed. In addition, we conducted a volatilization and sensory test for 60 days with the lid partially open, the toilet placed in a flush toilet with a volume of approximately 4m3 , and an average temperature of 15℃.
2.75 (value based on the 6-level odor intensity display method, hereinafter:
Expressed simply by numbers. (See Note 1) and volatilization rate (volatilization amount/total amount of volatile components, hereinafter simply abbreviated as volatilization rate) of 94%, very good results were obtained.
The gel residue after volatilization became darker in color, but still maintained its beautiful transparency. For comparison, a carrageenan-based aqueous gel fragrance volatile material (carrageenan powder 2.2 g, sea surfactant 1.1 g) was poured into the container used in this example, cooled, and gelled.
Osmanthus osmanthus blend fragrance 8.8g, water 97.9g, total 110g)
Volatilization and sensory tests were carried out under exactly the same conditions as for the SBC gel mentioned above, but the volatilization rate reached 96% as early as 30 days, and the appearance was completely shrunk and dried. was 4.25 to 2.75. Example 2 10 parts of S-E・B-S (trade name) Kraton G-1651 manufactured by Shell Chemical Co., Ltd. was placed in a suitable container, and isoparaffin (manufactured by Shell Chemical Co., Ltd., trade name Add 90 parts of Shellsol 71) and melt while heating and stirring until it becomes a completely transparent and highly viscous solution at 140℃, then pour 65g of this into a pull-top can with a diameter of 75mm, depth of 23mm, and capacity of 100c.c. death,
Wait for it to slowly cool at room temperature until it becomes a completely transparent gel, then add 5g of an osmanthus-based blended fragrance colored orange with an orange oil-soluble dye.
The bottom of the can was closed using a sealing machine. After leaving this filled sealed can at room temperature for 72 hours, when you open the can from the pull-top side, the fragrance is completely absorbed into the gel body to the point where your fingers won't get wet even if you touch it with your hands. The finished product was a completely transparent, highly elastic, aromatic gel body. Volatilization and sensory tests were conducted on this aromatic gel body in an opened can, placed in a flush toilet with a volume of approximately 4m3 , at an average temperature of 15℃, for 60 days, and the aroma intensity within the period was 3.5 to 2.5, and the volatilization rate was 78%. After the results are obtained, the shrinkage gel body left in the can is still 10-20
It was in a state where the aroma could be evaporated for several days, and it still retained its original beautiful transparency. Example 3 The empty air freshener container used in Example-1 was filled with S-B-S (trade name: Califrex TR-) manufactured by Ciel Chemical.
1184, styrene/rubber ratio 30/70, molecular weight 150000)
Filled with 22g (20 parts) of powder (not more than 16 mesh),
Add to this 79.2 g (72 parts) of isoparaffin (trade name: Shellsol 71 manufactured by Shell Chemical Co., Ltd.) with an initial distillation temperature of 174°C and a dry point of 207°C.
And, it was colored pale green in advance with green oil-soluble dye,
Mixed solution with 8.8g (8 parts) of green apple-based blended fragrance
Inject 88g (80 parts), degas with 100mm of mercury, seal tightly, and leave to warm in a constant temperature bath adjusted to 70℃ for 45 minutes (content temperature at 45th minute is 68℃). When I waited for it to cool to room temperature and removed the lid, I found a light green, almost transparent, highly elastic, aromatic gel. Regarding this aromatic gel body in a container, under the condition that the container is upside down,
A 24-hour abuse test was conducted at 50°C and -10°C, but no gel flow or deformation due to high temperatures or syneresis due to low temperatures was observed. In addition, the lid is half open, the flush toilet has a volume of approximately 4m3 , the average temperature is 15℃, and the number of days is 60.
A day-long volatilization and sensory test was conducted, and very good results were obtained, with an aroma intensity of 4.0 to 2.75 and a volatilization rate of 92%. The gel residue after volatilization became darker in color, but still maintained its original transparency. Example 4 In a suitable container, S-I-S manufactured by Shell Chemical Co., Ltd. (trade name Califrex TR-1111, styrene/rubber ratio
21/79, molecular weight 100000), and add the first distillation to this.
Add 75 parts of isoparaffin (Shell Sol 71, manufactured by Shell Chemical Co., Ltd., trade name) with a temperature of 174°C and a dry point of 207°C, and melt it while heating and stirring. When it becomes an almost transparent and highly viscous solution at 130°C, this is added. Pour 65g into a pull-top can with a diameter of 75mm, a depth of 23mm, and a capacity of 100c.c.
The mixture was slowly cooled at room temperature until it became an almost transparent, highly elastic gel, then 5 g of a lemon-based blended fragrance colored yellow with a yellow oil-soluble dye was added, and the bottom of the can was closed using a sealing machine. After leaving the filled sealed can at room temperature for 72 hours, when the can is opened from the pull-top side, the fragrance has been completely absorbed into the gel body to the point where even if you touch it with your fingers, your fingers won't get wet at all. The finished product was a yellow, almost transparent, highly elastic aromatic gel.
Volatilization and sensory tests were conducted on this aromatic gel body in an opened can, placed in a flush toilet with a volume of approximately 4 m 3 at an average temperature of 15°C for 60 days, and the aroma intensity within the period was 3.5 to 2.5, with a volatilization rate of 76. %, and the shrunken gel body remaining in the can was still in a state where the aroma could be volatilized for about 10 to 20 days, and still maintained its original transparency. Example 5 4 parts of powder of S-E・B-S (trade name: Kraton G-1651 manufactured by Ciel Chemical Co., Ltd.) was placed in a suitable container, and to this was added isoparaffin (manufactured by Ciel Chemical Co., Ltd.) with an initial distillation temperature of 174°C and a dry point of 207°C. A mixture of 86 parts of Shellsol (trade name: Shellsol 71) and 10 parts of an osmanthus-based blended fragrance that has been previously colored orange with an orange-based oil-soluble dye is added, and the mixture is heated and stirred until melted. It became a highly viscous solution. This is 75mm in diameter and 23mm in depth.
When 65g of the product was poured into a pull-top can with a capacity of 100c.c. and slowly cooled at room temperature, it became an orange, completely transparent, highly elastic, aromatic gel, although its strength decreased slightly. In this state, volatilization and sensory tests were conducted in a flush toilet with a volume of approximately 4 m 3 at an average temperature of 15°C for 60 days.The volatilization rate was 96%, and the aroma intensity during the period was 3.5 to 2.75.
The result was obtained. The gel residue after volatilization still maintained its original transparency. 【table】

Claims (1)

【特許請求の範囲】 1 液状脂肪族炭化水素をスチレン系熱可塑性エ
ラストマーでゲル化してなる透明ゲル状物とその
中に含有させた香料とからなることを特徴とする
透明ゲル状香料揮散体。 2 液状脂肪族炭化水素が100℃より高い沸点を
有する特許請求の範囲第1項に記載の透明ゲル状
香料揮散体。 3 スチレン系熱可塑性エラストマー含量が5〜
25重量%である特許請求の範囲第1項又は第2項
に記載の透明ゲル状香料揮散体。 4 予め香料を溶解させた液状脂肪族炭化水素に
スチレン系熱可塑性エラストマーの粉末を分散さ
せ、香料を劣化せしめない温度条件下に該分散物
を透明ゲル化一体物になるに十分な時間静置せし
めることを特徴とする透明ゲル状香料揮散体の製
造法。
[Scope of Claims] 1. A transparent gel-like fragrance volatile material comprising a transparent gel-like material formed by gelling a liquid aliphatic hydrocarbon with a styrene-based thermoplastic elastomer, and a fragrance contained therein. 2. The transparent gel-like fragrance volatile material according to claim 1, wherein the liquid aliphatic hydrocarbon has a boiling point higher than 100°C. 3 Styrenic thermoplastic elastomer content is 5~
The transparent gel-like fragrance volatile material according to claim 1 or 2, which has a content of 25% by weight. 4 Disperse powder of styrenic thermoplastic elastomer in liquid aliphatic hydrocarbon in which fragrance has been dissolved in advance, and leave the dispersion to stand for a sufficient time to form a transparent gelled solid under temperature conditions that do not deteriorate the fragrance. 1. A method for producing a transparent gel-like fragrance volatile material.
JP60175758A 1985-08-12 1985-08-12 Transparent gel like aroma volatilizing body and its production Granted JPS6238166A (en)

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JP60175758A JPS6238166A (en) 1985-08-12 1985-08-12 Transparent gel like aroma volatilizing body and its production

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Application Number Priority Date Filing Date Title
JP60175758A JPS6238166A (en) 1985-08-12 1985-08-12 Transparent gel like aroma volatilizing body and its production

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Publication Number Publication Date
JPS6238166A JPS6238166A (en) 1987-02-19
JPH0563184B2 true JPH0563184B2 (en) 1993-09-10

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Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62249652A (en) * 1986-03-27 1987-10-30 花王株式会社 Gel like aroma composition
JPS62249653A (en) * 1986-04-10 1987-10-30 花王株式会社 Gel like aroma composition
GB0009577D0 (en) * 2000-04-19 2000-06-07 Reckitt & Colmann Prod Ltd Improvements in or relating to organic compositions
GB2372447B (en) * 2001-02-21 2005-02-02 Jeyes Group Ltd Air fresheners
JP2005218761A (en) * 2004-02-09 2005-08-18 Seed Co Ltd Perfume-containing gel

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JPS6238166A (en) 1987-02-19

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