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JPS588292B2 - Preparation method of microcapsules - Google Patents
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JPS588292B2 - Preparation method of microcapsules - Google Patents

Preparation method of microcapsules

Info

Publication number
JPS588292B2
JPS588292B2 JP53026895A JP2689578A JPS588292B2 JP S588292 B2 JPS588292 B2 JP S588292B2 JP 53026895 A JP53026895 A JP 53026895A JP 2689578 A JP2689578 A JP 2689578A JP S588292 B2 JPS588292 B2 JP S588292B2
Authority
JP
Japan
Prior art keywords
polymer
microcapsules
solvent
solution
core substance
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
JP53026895A
Other languages
Japanese (ja)
Other versions
JPS54119373A (en
Inventor
小林晴己
上林明
大淵薫
鈴木英雄
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP53026895A priority Critical patent/JPS588292B2/en
Publication of JPS54119373A publication Critical patent/JPS54119373A/en
Publication of JPS588292B2 publication Critical patent/JPS588292B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/06Making microcapsules or microballoons by phase separation
    • B01J13/14Polymerisation; cross-linking
    • B01J13/16Interfacial polymerisation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Preparation (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Description

【発明の詳細な説明】 本発明は芯物質を高分子の殼皮で包蔵したマイクロカプ
セルの調製方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preparing microcapsules in which a core substance is encapsulated in a polymer shell.

従来、酵素、医薬品などの生理活性物質及びその他の化
学薬剤をマイクロカプセル化する方法としては、有機溶
媒からの相分離法、界面沈殿法、界面重合法などが知ら
れているが未だ満足すべきものではなかった。
Conventionally, known methods for microencapsulating physiologically active substances such as enzymes, pharmaceuticals, and other chemical agents include phase separation from organic solvents, interfacial precipitation, and interfacial polymerization, but these methods are still unsatisfactory. It wasn't.

たとえば相分離法では、コアセルベーション領域で界面
に適当な厚さの相分離を起こさせる条件の設定に著しい
困難が伴い、相分離状態において高分子希薄層に分配さ
れて損失分となる高分子が多いという欠点がある。
For example, in the phase separation method, it is extremely difficult to set the conditions to cause phase separation to an appropriate thickness at the interface in the coacervation region. The disadvantage is that there are many

また界面沈殿法では、二次エマルジョンの安定は生成条
件の設定が困難で、マイクロカプセル化率が低くなり易
いという問題がある。
Further, in the interfacial precipitation method, there is a problem that it is difficult to set the generation conditions to stabilize the secondary emulsion, and the microencapsulation rate tends to be low.

さらには、これら二種の方法では、得られるマイクロカ
プセル殼皮は有機溶媒を含む液体膜状であって強度やカ
?セル芯物質の保持力を高めるためにも架橋剤処理等を
必要とする場合が多い。
Furthermore, in these two methods, the microcapsule shells obtained are in the form of a liquid film containing an organic solvent, so they have poor strength and strength. In many cases, treatment with a crosslinking agent or the like is required to increase the retention force of the cell core material.

この場合、芯物質が架橋剤に敏感なものであるときには
、その架橋剤処理により芯物質が阻害されるという問題
が生じる。
In this case, if the core material is sensitive to the crosslinking agent, a problem arises in that the core material is inhibited by treatment with the crosslinking agent.

界面重合法では、反応性単量体と芯物質との相互作用を
回避することはできず、化学的に敏感な生理活性物質の
マイクロカプセル化には不適当であるし、またこの方法
では、界面に対する単量体の浸透が制約されるため、原
理上薄い膜厚のカプセルしか得られないという欠点があ
る。
Interfacial polymerization cannot avoid the interaction between reactive monomers and core substances, making it unsuitable for microencapsulation of chemically sensitive physiologically active substances. Since the permeation of the monomer to the interface is restricted, there is a drawback that in principle only capsules with a thin film thickness can be obtained.

本発明者らは前記したような従来のマイクロカプセル化
技術における欠点を克服し、芯物質の生理学的及び化学
的活性を損わずに、機械的強度の良好なマイクロカプセ
ルを工業上有利に調製し得る方法を開発すべく鋭意研究
を重ねた結果、親水性高分子を基体とし、これに疎水性
光感応基が結;合した光架橋性高分子を殼皮としてあら
かじめ形成した芯物質未包蔵のマイクロカプセル基体に
対し、芯物質を溶液状で含浸させたのち、光照射して該
高分子を光感応基を介して光架橋化することによって、
前記目的を達成し得ることを見出し、i本発明を完成す
るに到った。
The present inventors overcame the drawbacks of the conventional microencapsulation techniques as described above, and industrially advantageously prepared microcapsules with good mechanical strength without impairing the physiological and chemical activities of the core substance. As a result of intensive research to develop a method that can be used as a shell material, we have developed a method that uses a hydrophilic polymer as a base material and has a hydrophobic photosensitive group attached to it. By impregnating the microcapsule substrate with a core substance in a solution form, and then irradiating it with light to photocrosslink the polymer via the photosensitive group,
The inventors have discovered that the above object can be achieved and have completed the present invention.

本発明において、マイクロカプセルの殼皮材料として用
いる高分子は、親水性高分子を基体としこれに疎水性光
感応基が結合した構造を有する有機溶媒可溶性のもので
ある。
In the present invention, the polymer used as the shell material of the microcapsule is an organic solvent-soluble polymer having a structure in which a hydrophilic polymer is used as a base and a hydrophobic photosensitive group is bonded to the base.

この場合の親水性高分子基体としては、ポリビニルアル
コール、ポリアクリル酸、ポリアクリルアミド、ポリヒ
ドロキシアルキルメクアクリレート、ポリアミノ酸、多
,糖類、ムコ多糖類、タンパク質など分子中にヒドロキ
シル基や、アミン基、カルボキシル基、アミド基などの
親水基を有するものが挙げられる。
In this case, the hydrophilic polymer substrates include polyvinyl alcohol, polyacrylic acid, polyacrylamide, polyhydroxyalkylmethacrylate, polyamino acids, polysaccharides, mucopolysaccharides, proteins, etc., which have hydroxyl groups, amine groups, etc. Examples include those having hydrophilic groups such as carboxyl groups and amide groups.

またこれに結合する疎水性光感応基としては、2−フリ
ルアクリロイル基、メタクロイル基、シンナモイル基、
α−シアノシンナミリデン酢酸エステル基、p−アジド
ベツゾイル基、α−シアノーp−アジドシンナモイル基
、p−フエニレンジアクリロイル基等の不飽和カルボキ
シロイル基などを挙げることができる。
In addition, examples of the hydrophobic photosensitive group bonded to this include a 2-furyl acryloyl group, a methacryloyl group, a cinnamoyl group,
Examples include unsaturated carboxyloyl groups such as α-cyanocinnamylidene acetate group, p-azidobetzoyl group, α-cyano p-azidocinnamoyl group, and p-phenylene diacryloyl group.

これらの疎水性光感応基と親・水性基体高分子との結合
は高分子の親水性基を介して行うことができる。
These hydrophobic photosensitive groups can be bonded to the hydrophilic/aqueous base polymer via the hydrophilic groups of the polymer.

また本発明において用いる光架橋性高分子は、その親水
性と疎水性の調節を図るために別に長鎖飽和力ルポキシ
ロイル基やホスホリル基、スルフオニル基、第四アンモ
ニウシム基などのイオン解離基を適宜導入することもで
きる。
In addition, in order to adjust the hydrophilicity and hydrophobicity of the photocrosslinkable polymer used in the present invention, ionically dissociable groups such as long-chain saturating lupoxyloyl groups, phosphoryl groups, sulfonyl groups, and quaternary ammonium sium groups are added as appropriate. It can also be introduced.

本発明において好ましく用いられる光架橋性高分子は、
入手容易性から、ポリビニルアルコール、アミロース、
デンプン、アルギン酸等の部分的な,シンナモイルエス
テル、シンナミリデン酢酸エステル、α−シアノシンナ
ミリデン酢酸エステルなどがあげられる。
The photocrosslinkable polymer preferably used in the present invention is
Due to easy availability, polyvinyl alcohol, amylose,
Examples include partial cinnamoyl ester, cinnamylidene acetate, α-cyanocinnamylidene acetate, etc. of starch, alginic acid, etc.

本発明の方法を実施するには、まず、芯物質を包蔵しな
いマイクロカプセル基体を作る。
To carry out the method of the present invention, first, a microcapsule substrate that does not encapsulate a core substance is prepared.

このも、のの調製法は特に制約されず、従来公知の方法
を利用することもできるが、本発明の場合は、前記した
高分子物質の特性を利用し、油中水滴型又は水中油滴型
の乳化液を得るために、この高分子物質を溶解する溶液
と、この溶液に対し非混オロ性又,は非相溶性の溶媒を
激しくかきまぜて、乳化処理するのがよい。
In this case, the preparation method is not particularly limited, and conventionally known methods can be used, but in the case of the present invention, water-in-oil or oil-in-water type In order to obtain a type of emulsion, it is preferable to carry out emulsification treatment by vigorously stirring a solution in which the polymeric substance is dissolved and a solvent that is immiscible or immiscible with this solution.

この場合、高分子溶液を形成するための溶媒と、これに
添加する溶媒は相互に非混和性のものである。
In this case, the solvent for forming the polymer solution and the solvent added thereto are mutually immiscible.

この有機溶媒としてハ、タトえば、芳香族、脂肪族、脂
環族の炭化水素系溶媒・又はそれらのハロゲン化物など
が挙げられる。
Examples of this organic solvent include aromatic, aliphatic, and alicyclic hydrocarbon solvents and their halides.

高分子溶液中の高分子濃度は、O.’0 1〜10重量
係、好ましくは0.05〜5重量係である。
The polymer concentration in the polymer solution is O. '0 1 to 10 weight ratio, preferably 0.05 to 5 weight ratio.

乳化処理温度はOO−常温、場合によっては加温が採用
される。
The emulsification treatment temperature is OO-room temperature, and in some cases, heating is employed.

乳化処理する場合、油中水滴型の乳化液を形成させるに
は、高分子の有機溶媒溶液に対して水又は水性溶媒を加
えて激しくかきまぜ、一方、水中油滴型の乳化液を形成
させるには、水又は水性媒体に対して、高分子の有機溶
媒溶液を加えて激しくかきまぜる。
In emulsification treatment, to form a water-in-oil emulsion, water or an aqueous solvent is added to a solution of a polymer in an organic solvent and stirred vigorously; Add a solution of a polymer in an organic solvent to water or an aqueous medium and stir vigorously.

また、この乳化魁理においては、慣用の乳化剤を使用す
ることができる。
Further, in this emulsification process, a commonly used emulsifier can be used.

分散媒中に分散する液滴の量は、通常、乳化液全体のo
.i〜10重量係である。
The amount of droplets dispersed in the dispersion medium is usually determined by the o
.. i~10 weight section.

このような乳化処理により、溶解する高分子は、その親
水性一疎水性のバランスにより分散媒と液滴との界面に
析出し、内部に溶媒を包蔵するマイクロカプセルが得ら
れる。
Through such emulsification treatment, the dissolved polymer is precipitated at the interface between the dispersion medium and the droplet due to its hydrophilic-hydrophobic balance, and microcapsules containing the solvent are obtained.

本発明において、このようにして得られたマイクロカプ
セルを分散媒から分離し、次に、芯物質を溶解する溶液
中に浸漬し、その芯物質をマイクロカプセルの殼皮を通
してその内部に含浸させる。
In the present invention, the microcapsules thus obtained are separated from the dispersion medium, and then immersed in a solution that dissolves the core material, and the core material is impregnated into the interior of the microcapsules through the shell.

この場合、マイクロカプセルは、殼皮が未架橋のもので
あるから、溶液中の芯物質を容易に内部に通過させる。
In this case, since the shell of the microcapsule is uncrosslinked, the core substance in the solution can easily pass through the microcapsule.

芯物質としては、酵素、ホルモン、医薬、農薬、化学薬
品、その他の種々の物質が採用される。
Enzymes, hormones, medicines, agricultural chemicals, chemicals, and other various substances are used as the core substance.

芯物質溶液中の芯物質濃度は特に制約されず、高濃度の
方がより迅速にマイクロカプセル内部へ浸透させ得るが
、一般的には、1〜50重量係程度である。
The concentration of the core substance in the core substance solution is not particularly limited, and the higher the concentration, the more quickly the core substance can penetrate into the inside of the microcapsule, but it is generally about 1 to 50% by weight.

本発明により、芯物質未包蔵のマイクロカプセル基体に
芯物質を含浸させる場合、その芯物質溶液の溶媒は、マ
イクロカプセル基体に包蔵されている溶媒に対し、混和
性又は相溶性のものが採用される。
According to the present invention, when a core substance is impregnated into a microcapsule substrate that does not contain a core substance, the solvent of the core substance solution is one that is miscible or compatible with the solvent encapsulated in the microcapsule substrate. Ru.

また、この芯物質の含浸を有利に行なうには、乳化工程
から分離されたマイクロカプセル基体を真空容器に入れ
、その内部に含まれている溶媒を除去し、次にこの容器
中に芯物質溶液を注入するのがよい。
In addition, in order to advantageously impregnate the core substance, the microcapsule substrate separated from the emulsification process is placed in a vacuum container, the solvent contained therein is removed, and then the core substance solution is placed in the container. It is better to inject.

この場合には、芯物質溶液の溶媒は制約されず、水溶性
、非水溶性の任意の溶媒とすることができ、また含浸■
時間も短かくてすむ。
In this case, the solvent for the core material solution is not restricted and can be any water-soluble or non-water-soluble solvent.
It also takes less time.

さらに、マイクロカプセル基体に含まれる溶媒が揮発性
のものである場合は、適当な時間大気中に放置し、ある
いは適度の加熱を併用することによって、その内部溶媒
を蒸発除去し、次に、芯物質溶液中に浸漬して芯物質を
含浸させることもできる。
Furthermore, if the solvent contained in the microcapsule substrate is volatile, the internal solvent is evaporated by leaving it in the air for an appropriate period of time or by applying appropriate heating, and then the core It is also possible to impregnate the core material by immersing it in a solution of the material.

このようにして芯物質を包蔵させたマイクロカプセルは
、光照射し、その殼皮を構成する高分子物質を、その光
架橋基を介して架橋化する。
The microcapsules encapsulating the core substance in this manner are irradiated with light to crosslink the polymeric substance constituting the shell through the photocrosslinking group.

この架橋化によって、包蔵された芯物質が内部に固定化
されたマイクロカプセルを得ることができる。
This crosslinking makes it possible to obtain microcapsules in which the encapsulated core substance is immobilized.

本発明において、乳化処理を行う場合、安定乳化液を得
るために必要に応じ適当な界面活性剤その他の乳化助剤
を添加することができる。
In the present invention, when performing emulsification treatment, appropriate surfactants and other emulsification aids may be added as necessary to obtain a stable emulsion.

また光照射処理を行う場合、照射光としては250nm
前後の紫外線から可視光線までの利用が可能であり、ま
たこの光照射処理に際しては、光架橋反応に慣用される
種々の増感剤、たとえばリボフラビンのヨウな水溶性増
感剤、2−ニトロフルオレン、5−ニトロアセナフテン
のような有機溶媒可溶性増感剤を任意に併用することが
できる。
In addition, when performing light irradiation treatment, the irradiation light is 250 nm.
It is possible to use both ultraviolet light and visible light, and for this light irradiation treatment, various sensitizers commonly used in photocrosslinking reactions, such as water-soluble sensitizers such as riboflavin, and 2-nitrofluorene, can be used. , 5-nitroacenaphthene, and other organic solvent-soluble sensitizers may optionally be used in combination.

本発明により得られるマイクロカプセルは殼反が光架橋
化した高分子からなるものであることから機械的強度は
大きく、また包蔵する芯物質の固定化を良好に達成する
ことができる。
Since the microcapsules obtained by the present invention have shells made of photo-crosslinked polymers, they have high mechanical strength and can achieve good immobilization of the encapsulated core substance.

さらに本発明によるマイクロカプセルの調製は実施容易
であり、その架橋化は光照射により行われるので従来の
架橋処理剤を用いる場合に見られるような芯物質の活性
低下など、損傷されるようなことはない。
Furthermore, the preparation of microcapsules according to the present invention is easy to carry out, and since the crosslinking is carried out by light irradiation, there is no possibility of damage such as a decrease in the activity of the core substance, which is seen when using conventional crosslinking agents. There isn't.

また、乳化液中の高分子濃度を適当に調節することによ
り、マイクロカプセルの殼皮を適当厚に調節することが
可能で、光照射量を変化させて芯物質の外部への漏洩あ
るいは透過度を変化させることが町能である。
In addition, by appropriately adjusting the polymer concentration in the emulsion, it is possible to adjust the thickness of the shell of the microcapsules to an appropriate thickness, and by changing the amount of light irradiation, it is possible to prevent leakage of the core substance to the outside or increase the permeability. Town Noh is about changing the world.

本発明1こよれば粒径10〜数百μmの範囲のマイクロ
カプセルを各易に得ることができ、その産業上の意義は
大きい。
According to the present invention, microcapsules having a particle size in the range of 10 to several hundred μm can be easily obtained, and its industrial significance is great.

次に本発明を実施例}こよりさらに詳細に説明する。Next, the present invention will be explained in more detail with reference to Examples.

実施例 1 平均重合度約1500のポリビニルアルコールに、ピリ
ジン中でゲイ皮酸クロリドを作用させて得られるケイ皮
酸エステル(エステル{tJ約o. 3 4 )250
mI?及び2−ニトローフルオレン10m9をク四ロホ
ルムーベンセンーヘキナン( 容積比: 3 :4:3
)の混合溶媒2001nlに溶かした溶液に水25TL
lを加え、水冷下乳化させる。
Example 1 Cinnamate ester (ester {tJ approx. o. 3 4 ) obtained by reacting polyvinyl alcohol with an average degree of polymerization of about 1500 with genamic acid chloride in pyridine 250
mI? and 10 m9 of 2-nitrofluorene to dichloroform-benzene-hequinane (volume ratio: 3:4:3
) in 2001nl of mixed solvent, add 25TL of water.
1 and emulsify under cooling with water.

この乳化液(油中水滴型)を4℃で遠心して上澄を除い
た後、10%ツイーン20水溶液200rrLlに加え
て攪拌し、さらに有機溶媒を除く。
This emulsion (water-in-oil type) was centrifuged at 4° C. to remove the supernatant, then added to 200 rrLl of a 10% Tween 20 aqueous solution, stirred, and the organic solvent was further removed.

水冷下2時間攪拌したのち、懸濁液にL−アスコルビ/
酸を5係濃度で溶かし、さらに水冷下2時間攪拌したの
ち、400W高圧水銀灯10分間照射する。
After stirring for 2 hours under water cooling, L-ascorby/
The acid was dissolved at a concentration of 5%, stirred for 2 hours under water cooling, and then irradiated with a 400W high-pressure mercury lamp for 10 minutes.

カプセルを口過して分離し、アスコルビン酸含有マイク
ロカプセルを得た。
The capsules were separated by mouth-passing to obtain ascorbic acid-containing microcapsules.

実施例 2 実施例1で示したケイ皮酸エステル50■をクロロホル
ム25mlに溶かす。
Example 2 50 ml of the cinnamate ester shown in Example 1 was dissolved in 25 ml of chloroform.

この高分子溶液に増感剤2−ニトロフルオレン10■を
加えたのち、これを20%ツイーン20水溶液250m
lに加えて乳化液(水中油滴型)として35゜Cで30
分間攪拌してクロロホルムの一部をとばす。
After adding 10 μm of sensitizer 2-nitrofluorene to this polymer solution, this was mixed with 250 m of a 20% Tween 20 aqueous solution.
30°C at 35°C as an emulsion (oil-in-water type) in addition to
Stir for a minute to evaporate some of the chloroform.

この乳化液を遠心して上澄を除いたのち、カプセル層を
10gのイソプロビルーN−(3−クロロフエニル)カ
ルバメートヲ含むクロロホルムーベンゼンーヘキサン(
容量比:1:4:5)混合溶媒100dに懸濁し、水冷
下30分間攪拌したのち、400W高圧水銀灯で5分間
光照射したのち、遠心分離して、インプロピルーN−(
3−クロロフエニル).カルバメート包蔵マイクロカプ
セルを得た。
After centrifuging this emulsion and removing the supernatant, the capsule layer was separated into chloroform-benzene-hexane (containing 10 g of isoprobyl-N-(3-chlorophenyl) carbamate).
Volume ratio: 1:4:5) was suspended in 100 d of mixed solvent, stirred for 30 minutes under water cooling, irradiated with light for 5 minutes using a 400W high-pressure mercury lamp, centrifuged, and inpropyru N-(
3-chlorophenyl). Carbamate-containing microcapsules were obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 親水性高分子を基体とし、これに疎水性光感応基が
結合した光架橋性高分子を殼皮としてあらかじめ形成し
た芯物質未包蔵のマイクロカプセル基体に対し、芯物質
溶剤を含浸させたのち、光照射して該高分子を光感応基
を介して光架橋化し、含浸芯物質を固定化することを特
徴とするマイクロカプセルの調製方法。
1 After impregnating a core material solvent into a microcapsule substrate that does not contain a core material and is made of a hydrophilic polymer as a base material and a shell of a photocrosslinkable polymer with a hydrophobic photosensitive group bonded to the shell. . A method for preparing microcapsules, which comprises irradiating light to photo-crosslink the polymer via a photosensitive group to immobilize the impregnated core material.
JP53026895A 1978-03-09 1978-03-09 Preparation method of microcapsules Expired JPS588292B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53026895A JPS588292B2 (en) 1978-03-09 1978-03-09 Preparation method of microcapsules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53026895A JPS588292B2 (en) 1978-03-09 1978-03-09 Preparation method of microcapsules

Publications (2)

Publication Number Publication Date
JPS54119373A JPS54119373A (en) 1979-09-17
JPS588292B2 true JPS588292B2 (en) 1983-02-15

Family

ID=12205974

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53026895A Expired JPS588292B2 (en) 1978-03-09 1978-03-09 Preparation method of microcapsules

Country Status (1)

Country Link
JP (1) JPS588292B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6142192U (en) * 1984-08-20 1986-03-18 オンキヨー株式会社 speaker
US10059898B2 (en) 2015-08-21 2018-08-28 Exxonmobil Chemical Patents Inc. High-viscosity metallocene polyalpha-olefins with high electrohydrodynamic performance
US10611980B2 (en) 2015-10-15 2020-04-07 Exxonmobil Chemical Patents Inc. Lubricant containing high-viscosity metallocene polyalpha-olefins
US10731096B2 (en) 2015-08-21 2020-08-04 Exxonmobil Chemical Patents Inc. Lubricant base stock blends

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4683092A (en) * 1985-07-03 1987-07-28 Damon Biotech, Inc. Capsule loading technique
JPH02258053A (en) * 1989-03-31 1990-10-18 Mita Ind Co Ltd Preparation of single nucleus hydrated microcapsule
CA2311195A1 (en) * 2000-06-12 2001-12-12 Mcmaster University Photostimulated phase separation encapsulation
EP1414561A2 (en) * 2001-08-03 2004-05-06 Maripro AS Improvements in or relating to encapsulation

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5322581A (en) * 1976-08-13 1978-03-02 Ishii Hideki Porous fine particle and preparation thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6142192U (en) * 1984-08-20 1986-03-18 オンキヨー株式会社 speaker
US10059898B2 (en) 2015-08-21 2018-08-28 Exxonmobil Chemical Patents Inc. High-viscosity metallocene polyalpha-olefins with high electrohydrodynamic performance
US10731096B2 (en) 2015-08-21 2020-08-04 Exxonmobil Chemical Patents Inc. Lubricant base stock blends
US10611980B2 (en) 2015-10-15 2020-04-07 Exxonmobil Chemical Patents Inc. Lubricant containing high-viscosity metallocene polyalpha-olefins

Also Published As

Publication number Publication date
JPS54119373A (en) 1979-09-17

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