JPH0217938A - Preparation of microcapsule - Google Patents

Preparation of microcapsule

Info

Publication number
JPH0217938A
JPH0217938A JP63167486A JP16748688A JPH0217938A JP H0217938 A JPH0217938 A JP H0217938A JP 63167486 A JP63167486 A JP 63167486A JP 16748688 A JP16748688 A JP 16748688A JP H0217938 A JPH0217938 A JP H0217938A
Authority
JP
Japan
Prior art keywords
hydrophobic substance
melamine
leuco dye
aqueous dispersant
copolymer
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.)
Granted
Application number
JP63167486A
Other languages
Japanese (ja)
Other versions
JP2679129B2 (en
Inventor
Hiroshi Horiuchi
堀内 博司
Hirobumi Tsuka
塚 博文
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP63167486A priority Critical patent/JP2679129B2/en
Publication of JPH0217938A publication Critical patent/JPH0217938A/en
Application granted granted Critical
Publication of JP2679129B2 publication Critical patent/JP2679129B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • B01J13/18In situ polymerisation with all reactants being present in the same phase

Abstract

PURPOSE:To eliminate the generation of a large capsule of an air bubble by dispersing a hydrophobic substance having a leuco dye dissolved therein in a specific aqueous dispersant solution in an emulsified state and adding a melamine/formaldehyde precondensate thereto to heat the solution. CONSTITUTION:Dimethylpolysiloxane, a nonionic surfactant and synthetic silica are together used along with a copolymer of styrenes, which contain a compound represented by formula I(wherein R1 and R2 are a hydrogen atom or a 1-4C alkyl group and not simultaneously a hydrogen atom), and maleic anhydride to prepare an aqueous dispersant solution. After a hydrophobic substance having a colorless or light-colored leuco dye dissolved therein is emulsified and dispersed in the aforementioned aqueous dispersant solution, a melamine/ formaldehyde precondensate or a urea/formaldehyde precondensate is added to the obtained dispersion. Next, the formed composition is heated and reacted under acidic condition to prepare a microcapsule having the hydrophobic substance as a core substance.

Description

【発明の詳細な説明】 〈産業上の利用公費〉 本発明はロイコ染料を溶解した疎水性物質を内包する感
圧記録紙用マイクロカプセルの製法に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Utilization Public Funds> The present invention relates to a method for producing microcapsules for pressure-sensitive recording paper containing a hydrophobic substance in which a leuco dye is dissolved.

〈従来の技術〉 従来、マイクロカプセルを製造する際において使用され
る疎水性芯物質を分散させる分散剤としては、スチレン
−無水ケレイン酸共重合体(特公昭58−88116.
特開昭59−177128 )などの無水マレイン酸系
共重合体やスチレンスルフォン酸系共重合体(特開昭5
8−14912)などが一般奢ζ知られている。
<Prior Art> Conventionally, as a dispersant for dispersing a hydrophobic core substance used in manufacturing microcapsules, styrene-keleic anhydride copolymer (Japanese Patent Publication No. 58-88116.
Maleic anhydride copolymers such as JP-A-59-177128) and styrene sulfonic acid-based copolymers (JP-A-59-177128)
8-14912) etc. are commonly known.

しかし、従来知られているこれら分散剤を用いて、ロイ
コ染料を溶解した疎水性物質を分散させ、メラミン−ホ
ルムアルデヒド初期縮合物または尿素−ホルムアルデヒ
ド初期縮合物を加え、酸性条件下で加熱反応させてマイ
クロカプセルを製造した場合、分散性が不十分であり、
その結果、未カプセルが増え、マイクロカプセル化率が
低下する。また分散剤とロイコ染料が一部反応して液発
色が見られたりし、満足いくマイクロカプセルが得られ
なかった。
However, using these conventionally known dispersants, a hydrophobic substance in which a leuco dye is dissolved is dispersed, a melamine-formaldehyde initial condensate or a urea-formaldehyde initial condensate is added, and the mixture is heated and reacted under acidic conditions. When microcapsules are manufactured, their dispersibility is insufficient;
As a result, the amount of unencapsulated particles increases and the microencapsulation rate decreases. In addition, the dispersant and leuco dye partially reacted, causing color development in the liquid, making it impossible to obtain satisfactory microcapsules.

本発明者らはマイクロカプセルを製造する際、未カプセ
ルを極力抑え、また液発色を起こさない分散剤について
検討し、分散剤として核アルキル置換α−アルキルスチ
レンを必須成分とするスチレン類と無水マレイン酸との
共重合体を用いる方法(特開昭62−125851号)
、および分散剤としてα−メチルスチレンを必須成分と
するスチレン類と無水マレイン酸との共重合体を用いる
方法(特′91昭62−269742号)を見出した。
When producing microcapsules, the present inventors investigated dispersants that minimize uncapsules and do not cause liquid color development, and used styrenes containing nuclear alkyl-substituted α-alkylstyrene as an essential component and maleanhydride as dispersants. Method using copolymer with acid (JP-A-62-125851)
, and a method using a copolymer of styrenes and maleic anhydride containing α-methylstyrene as an essential component as a dispersant (Special Patent No. '91 Sho 62-269742).

〈発明が解決しようとする課題〉 しかしながらこれら分散剤を用いて乳化分散を行なった
場合分散性は優れるものの、発泡が多く、乳化分散時の
液体禎が増したり、気泡の巨大カプセルができたりして
未だ不十分であった。又発泡を抑制するためには、消泡
剤の添加が考えられるが、通常用いられているシリコン
系消泡剤では塗工時のハジキ等のトラブルが発生する。
<Problems to be Solved by the Invention> However, when emulsifying and dispersing using these dispersants, although the dispersibility is excellent, there is a lot of foaming, the liquid content during emulsifying and dispersing increases, and giant capsules of air bubbles are formed. was still insufficient. In order to suppress foaming, it is possible to add an antifoaming agent, but the commonly used silicone antifoaming agents cause problems such as repellency during coating.

〈課題を解決するための手段〉 本発明者らはロイコ染料を溶解した疎水性物質を効率良
く分散させ、かつ発泡を抑制し気泡の巨大カプセルの発
生をなくする方法を検討した結果、特定の分散剤と特定
のシリコン系消泡剤を併用することにより、未カプセル
を抑制しかつ発泡によるトラブルをなくしたマイクロカ
プセル分散液が得られ、さらに通常のシリコン系消泡剤
で見られる塗工時のハジキ等のトラブルがないことを見
出し本発明を完成した。
<Means for Solving the Problems> The present inventors have studied a method for efficiently dispersing a hydrophobic substance in which a leuco dye is dissolved, suppressing foaming, and eliminating the generation of giant capsules of air bubbles. By using a dispersant and a specific silicone antifoaming agent in combination, a microcapsule dispersion can be obtained that suppresses uncapsule formation and eliminates the troubles caused by foaming, and also reduces the problem during coating that occurs with ordinary silicone antifoaming agents. They found that there were no problems such as repellency and completed the present invention.

すなわち本発明は、無色ないし淡色のロイコ染料を溶解
した疎水性物質を分散剤水溶液中に乳化分散させた後、
メラミン−ホルムアルデヒド初期縮合物または尿素−ホ
ルムアルデヒド初期縮合物を添加し、酸性条件下で加熱
反応させて疎水性物質を芯物質゛としたマイクロカプセ
ルを製造する方法において、該分散剤として一般式(1
)で表わされる化合物を必須成分とするスチレン類と無
水マレイン酸との共重合体を用い、かつジメチルポリシ
ロキサン、ノニオン系界面活性剤および合成シリカを必
須成分とするシリコン系消泡剤を併用する仁とを特徴と
するマイクロカプセルの製法を提供するものである。
That is, in the present invention, after emulsifying and dispersing a hydrophobic substance in which a colorless or light-colored leuco dye is dissolved in an aqueous dispersant solution,
In a method for producing microcapsules with a hydrophobic substance as a core material by adding a melamine-formaldehyde initial condensate or a urea-formaldehyde initial condensate and carrying out a heating reaction under acidic conditions, the dispersant is a compound of the general formula (1).
) using a copolymer of styrenes and maleic anhydride that contains the compound represented by () as an essential component, and also uses a silicone antifoaming agent that contains dimethylpolysiloxane, a nonionic surfactant, and synthetic silica as essential components. The present invention provides a method for producing microcapsules characterized by:

〔式中、R1−R1は水素原子又はC1〜4のアルキル
基を表わし、かつ、Rt e R1は同時に水素原子で
はない。〕 一般式α)で表わされる化合物としては、α−メチルス
チレン、核メチル置換α−メチルスチレン、核エチル置
換α−メチルスチレン、核イソプロピル置換α−メチル
スチレン、ビニルトルエンなどが挙げられる。一般式(
1)で表わされる化合物と同時に、他のスチレン類を使
用することができるが、この他のスチレン類として代表
的なものはスチレンである。
[In the formula, R1-R1 represents a hydrogen atom or a C1-4 alkyl group, and Rte and R1 are not hydrogen atoms at the same time. ] Examples of the compound represented by the general formula α) include α-methylstyrene, nuclear methyl-substituted α-methylstyrene, nuclear ethyl-substituted α-methylstyrene, nuclear isopropyl-substituted α-methylstyrene, and vinyltoluene. General formula (
Other styrenes can be used simultaneously with the compound represented by 1), and styrene is a typical example of the other styrenes.

一般式(1)で表わされる化合物の使用態は、スチレン
類全量中lθモル%以上好ましくは、80モル%以上が
よい。
The usage of the compound represented by the general formula (1) is lθ mol% or more, preferably 80 mol% or more based on the total amount of styrenes.

これらスチレン類と無水マレイン酸との共重合反応は公
知の方法で行われ、例えば、アセトン、メチルエチルケ
トン、メチルイソブチルケトンなどの共重合体をも溶解
する溶剤中で行われたす、ベンゼン、トルエン、キシレ
ンなどの共重合体を析出させる溶剤中で行われたりする
方法がある。このようにして得られた該共重合体は固体
もしくは粉体の場合アンモニア水溶液、水酸化ナトリウ
ムなどのアルカリ金属の水溶液、またはモノメチルアミ
ン、ジメテルア疋ンなどの有機アミンの水溶液で水溶化
される。また溶剤に溶解した状態や溶剤を含有する場合
、前記のアンモニア、アルカリ金属、有機アミンの水溶
液を加え、溶剤と水とを置換する方法で水溶化される。
The copolymerization reaction of these styrenes and maleic anhydride is carried out by a known method, for example, in a solvent that also dissolves the copolymer such as acetone, methyl ethyl ketone, methyl isobutyl ketone, benzene, toluene, There is a method in which the copolymer is precipitated in a solvent such as xylene. When the copolymer thus obtained is a solid or powder, it is water-solubilized with an aqueous solution of ammonia, an aqueous solution of an alkali metal such as sodium hydroxide, or an aqueous solution of an organic amine such as monomethylamine or dimethylamine. When dissolved in a solvent or containing a solvent, it is made water-solubilized by adding an aqueous solution of ammonia, an alkali metal, or an organic amine to replace the solvent with water.

かくして得られた一般式(1)の化合物を必須成分とす
るスチレン類と無水マレイン酸との共重合体の水溶液を
ロイコ染料を溶解した疎水性物質の分散剤として使用す
るが、分散剤の濃度としては、0.6ないし10重量パ
ーセントで用いられる。
The thus obtained aqueous solution of a copolymer of styrene and maleic anhydride containing the compound of general formula (1) as an essential component is used as a dispersant for a hydrophobic substance in which a leuco dye is dissolved, but the concentration of the dispersant is It is used in an amount of 0.6 to 10 weight percent.

本発明に用いられる特定のシリコン系消泡剤は、ジメチ
ルポリシロキサン、ノニオン系界面活性剤および合成シ
リカを必須成分とするものであるが、ジメチルポリシロ
キサン100部に対するノニオン系界面活性剤と合成シ
リカの配合比率は20部/6部ないし60部/20部で
あり、必要に応じて水が加えられたものである。
The specific silicone antifoaming agent used in the present invention contains dimethylpolysiloxane, a nonionic surfactant, and synthetic silica as essential components. The blending ratio is 20 parts/6 parts to 60 parts/20 parts, and water is added as necessary.

し このノニオン系界面活性剤とすてはポリエチレングリコ
ールアルキルエーテルが好ましい。この特定のシリコン
系消泡剤の添加量は乳化分散系に対して100〜800
0ppm好ましくは200〜2000ppmがよい。
The preferred nonionic surfactant is polyethylene glycol alkyl ether. The amount of this specific silicone antifoaming agent added is 100 to 800% to the emulsified dispersion system.
0 ppm, preferably 200 to 2000 ppm.

また本発明に用いられるロイコ染料としては、例えばト
リフェニルメタン系ロイコ染料、フルオラン系ロイコ染
料、スピロピラン系ロイコ染料などが挙げられる。マイ
クロカプセルを製造する方・法それ自体は既知であり、
たとえば本発明の分散剤水溶液を酸性条件下で用いて疎
水性物質を分散または乳化させた後、メラミン−ホルム
アルデヒド初期縮合物または尿素−ホルムアルデヒド初
期縮合物を加え、酸性、加熱下に反応させてマイクロカ
プセルを製造する。
Examples of the leuco dyes used in the present invention include triphenylmethane leuco dyes, fluoran leuco dyes, and spiropyran leuco dyes. The method of manufacturing microcapsules itself is known;
For example, after dispersing or emulsifying a hydrophobic substance using the dispersant aqueous solution of the present invention under acidic conditions, a melamine-formaldehyde initial condensate or a urea-formaldehyde initial condensate is added, and the microorganisms are reacted under acidic conditions and heating. Manufacture capsules.

〈発明の効果〉 本発明の製法によってマイクロカプセルを製造すると、
乳化分散時の発泡が抑制され、液体積の増加もなく、気
泡の巨大カプセルの生成のない高品質のマイクロカプセ
ルが得られ、かつ紙へ塗工した時のハジキも生じないも
のである。
<Effects of the invention> When microcapsules are produced by the production method of the present invention,
Foaming during emulsification and dispersion is suppressed, there is no increase in liquid volume, high quality microcapsules are obtained without the formation of giant capsules of air bubbles, and no repellency occurs when coated on paper.

〈実施例〉 以下実施例により説明する。<Example> This will be explained below using examples.

参考例1 温度計、攪拌機、還流冷却器、滴下口斗を備えた144
ツロフラスコにアセトンl O9t1無水マレイン酸6
6 F、スチレン7?、α−メチルスチレン71Fを仕
込み、攪拌下に70℃まで昇温する。次いで予めアセト
ン81.5Fにアソビスイソブチロニトリル8.6Fを
溶解した溶液を滴下口斗より1時間で滴下し、アセトン
還流下でさら番ζ7時間保温する。次に温度66℃で攪
拌下に8.896苛性ソーダ水溶液711fを滴下口斗
より1時間で滴下した後、アセトンの留去を行う。得ら
れた共重合体水溶液は、濃度調整を行い濃度20%、p
H6,o、粘度2oポイズの微温粘稠液体856tを得
た。樹脂液Aとする。
Reference Example 1 144 equipped with a thermometer, stirrer, reflux condenser, and dropping spout
Acetone 1 O9 t1 Maleic anhydride 6 in a Tulo flask
6 F, styrene 7? , α-methylstyrene 71F was charged, and the temperature was raised to 70° C. while stirring. Next, a solution prepared by dissolving 8.6 F of azobisisobutyronitrile in 81.5 F of acetone was added dropwise from the dropping spout over 1 hour, and the mixture was kept warm for 7 hours under refluxing acetone. Next, 711f of an 8.896 aqueous sodium hydroxide solution was added dropwise from the dropping spout over 1 hour under stirring at a temperature of 66°C, and then the acetone was distilled off. The obtained copolymer aqueous solution was adjusted to a concentration of 20%, p
856 tons of a slightly warm viscous liquid having a viscosity of 20 poise and H6,0 was obtained. Let's call it resin liquid A.

9参考例2〜4 表−1に示すモノマー組成及び中和率となるように無水
マレイン酸、α−メチルスチレン、核メチル置換α−メ
チルスチレン、スチレン及び苛性ソーダの量を変え、か
つ、表−1に示す濃度となるよう昏ζ、濃度調整の条件
を変えた以外は参考例1と同様に行ない共重合体水溶液
を得た。それぞれ樹脂液B〜Dとする。
9 Reference Examples 2 to 4 The amounts of maleic anhydride, α-methylstyrene, nuclear methyl-substituted α-methylstyrene, styrene, and caustic soda were changed so that the monomer composition and neutralization rate shown in Table-1 were obtained, and An aqueous copolymer solution was obtained in the same manner as in Reference Example 1, except that the conditions for copolymerization and concentration adjustment were changed to obtain the concentration shown in Example 1. They are referred to as resin liquids B to D, respectively.

実施例1 疎水性物質としてクリスタルバイオレットラクトン8.
6重量部をKMC−118(呉羽化学株製オイル)96
.5重量部に溶解したものを用いる。
Example 1 Crystal violet lactone as hydrophobic substance 8.
6 parts by weight of KMC-118 (oil manufactured by Kureha Chemical Co., Ltd.) 96
.. A solution of 5 parts by weight is used.

攪拌装置、温度計、還流冷却器をつけたII四ツ目フラ
スコに樹脂液A40f、水160tを加え60℃に加熱
攪拌する。酢酸にてpH6,0に調整し、消泡剤として
ジメチルポリシロキサン100部に対してポリエチレン
グリコールモノブチルエーテル86部および合成シリカ
10部を水146部化分散させたものを0.19 F添
加し、上記疎水性物質180Fを加え、乳化分散した。
Resin liquid A 40f and 160 t of water were added to a II four-eye flask equipped with a stirrer, a thermometer, and a reflux condenser, and the mixture was heated to 60° C. and stirred. The pH was adjusted to 6.0 with acetic acid, and 0.19 F of 86 parts of polyethylene glycol monobutyl ether and 10 parts of synthetic silica dispersed in 146 parts of water to 100 parts of dimethylpolysiloxane was added as an antifoaming agent. The above hydrophobic substance 180F was added and emulsified and dispersed.

この乳化分散液にス【レーズレジン618(住友化学工
業株メラミンーホルムアルデヒド初期結合物80%品)
80tと水60gとの水溶液を加え、60℃にて1時間
攪拌し、マイクロカプセルを得た。
Add to this emulsified dispersion liquid [Laze Resin 618 (Sumitomo Chemical Co., Ltd. melamine-formaldehyde initial bond product 80% product)]
An aqueous solution of 80 t and 60 g of water was added and stirred at 60° C. for 1 hour to obtain microcapsules.

得られたマイクロカプセルをコールタ−カウンターにて
粒度分布を測定したとζろ気泡の巨大カプセルは認めら
れなかった。
When the particle size distribution of the obtained microcapsules was measured using a Coulter counter, no giant capsules of zeta bubbles were observed.

また下記配合により塗工液とし、市販上質紙(坪[55
F/♂)に乾燥重量で4 W/lとなるように塗工し、
120℃で1分間乾燥させてマイクロカプセル塗工紙を
得た。
In addition, a coating liquid was prepared using the following formulation, and a commercially available high-quality paper (tsubo [55 tsubo]
F/♂) at a dry weight of 4 W/l,
It was dried at 120° C. for 1 minute to obtain microcapsule coated paper.

この塗工紙は、ハジキは全く認められなかった。No repellency was observed on this coated paper.

実施例2〜4 樹脂液Aのかわりに樹脂液B〜Dを用い、かつ消泡剤量
を変化させたこと以外は実施例−1と同様にして行い、
マイクロカプセルを作成して評価を行った。結果を実施
例−1と併せて表−2に示した。
Examples 2 to 4 The same procedure as Example 1 was carried out except that resin liquids B to D were used instead of resin liquid A and the amount of antifoaming agent was changed.
Microcapsules were created and evaluated. The results are shown in Table 2 together with Example 1.

比較例−1〜2 消泡剤を全く用いなかったり、ノニオン系界面活性剤の
比率がジメチルポリシロキサンに対して7%である市販
シリコン系消泡剤を用いることを除いては実施例−1と
同様に行った。結果を表−2に併せて示した。
Comparative Examples-1 to 2 Example-1 except that no antifoaming agent was used or a commercially available silicone antifoaming agent with a nonionic surfactant ratio of 7% to dimethylpolysiloxane was used. I did the same thing. The results are also shown in Table-2.

Claims (1)

【特許請求の範囲】 無色ないし淡色のロイコ染料を溶解した疎水性物質を分
散剤水溶液中に乳化分散させた後、メラミン−ホルムア
ルデヒド初期縮合物または尿素−ホルムアルデヒド初期
縮合物を添加し、酸性条件下で加熱反応させて疎水性物
質を芯物質としたマイクロカプセルを製造する方法にお
いて、該分散剤として一般式( I )で表わされる化合
物を必須成分とするスチレン類と無水マレイン酸との共
重合体を用い、かつジメチルポリシロキサン、ノニオン
系界面活性剤および合成シリカを必須成分とするシリコ
ン系消泡剤を併用することを特徴とするマイクロカプセ
ルの製法。 ▲数式、化学式、表等があります▼( I ) 〔式中、R_1、R_■は水素原子又はC_1_〜_4
のアルキル基を表わし、かつ、R_1、R_■は同時に
水素原子ではない。〕
[Claims] After emulsifying and dispersing a hydrophobic substance in which a colorless or light-colored leuco dye is dissolved in an aqueous dispersant solution, a melamine-formaldehyde initial condensate or a urea-formaldehyde initial condensate is added, and the mixture is treated under acidic conditions. A copolymer of styrenes and maleic anhydride containing a compound represented by the general formula (I) as an essential component as a dispersant in a method for producing microcapsules with a hydrophobic substance as a core material by heating reaction with 1. A method for producing microcapsules, characterized by using a silicone antifoaming agent containing dimethylpolysiloxane, a nonionic surfactant, and synthetic silica as essential components. ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) [In the formula, R_1 and R_■ are hydrogen atoms or C_1_ to_4
represents an alkyl group, and R_1 and R_■ are not hydrogen atoms at the same time. ]
JP63167486A 1988-07-04 1988-07-04 Manufacturing method of microcapsules Expired - Lifetime JP2679129B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5804298A (en) * 1991-10-25 1998-09-08 Minnesota Mining And Manufacturing Company Microcapsules with reduced shell wall permeability

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5804298A (en) * 1991-10-25 1998-09-08 Minnesota Mining And Manufacturing Company Microcapsules with reduced shell wall permeability

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