JPH01164433A - Production of microcapsule - Google Patents

Production of microcapsule

Info

Publication number
JPH01164433A
JPH01164433A JP62320900A JP32090087A JPH01164433A JP H01164433 A JPH01164433 A JP H01164433A JP 62320900 A JP62320900 A JP 62320900A JP 32090087 A JP32090087 A JP 32090087A JP H01164433 A JPH01164433 A JP H01164433A
Authority
JP
Japan
Prior art keywords
mol
microcapsules
capsule
melamine
acid
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
JP62320900A
Other languages
Japanese (ja)
Other versions
JPH078334B2 (en
Inventor
Shinsuke Irii
入井 伸介
Hiroshi Kumamoto
熊本 寛士
Tomoharu Shiozaki
塩崎 知晴
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.)
Kanzaki Paper Manufacturing Co Ltd
Original Assignee
Kanzaki Paper Manufacturing 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 Kanzaki Paper Manufacturing Co Ltd filed Critical Kanzaki Paper Manufacturing Co Ltd
Priority to JP62320900A priority Critical patent/JPH078334B2/en
Publication of JPH01164433A publication Critical patent/JPH01164433A/en
Publication of JPH078334B2 publication Critical patent/JPH078334B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • B01J13/18In situ polymerisation with all reactants being present in the same phase

Abstract

PURPOSE:To efficiently form microcapsules having superior core substance retentivity by polycondensing a precondensate of aminoaldehyde resin in the presence of an anionic copolymer contg. vinylsulfonic acid and an arom. vinyl compd. CONSTITUTION:An aq. soln. of a copolymer consisting of vinylsulfonic acid, an arom. vinyl compd. such as styrene and acrylic acid, etc., added to facilitate the progress of polymn. is adjusted to the acidic region of 3-6pH. A precondensate of melamine-formaldehyde resin such as a precondensate of methylated methylol melamine is added to the aq. soln. and they are stirred at a constant temp. and cooled to obtain an opal white dispersion liq. contg. microcapsules. The microcapsules have superior heat, moisture and solvent resistances and useful for printing ink, pressure sensitive copying paper, etc.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、疎水性芯物質を内包するマイクロカプセルの
製造方法に関し、特に芯物質の保持性に優れたカプセル
を極めて容易に製造し得る方法に関するものである。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a method for manufacturing microcapsules containing a hydrophobic core substance, and in particular a method for extremely easily manufacturing capsules that have excellent core substance retention properties. It is related to.

「従来の技術」 近年、マイクロカプセル化技術の進歩は著しく、カプセ
ル化物の使用分野も感圧複写紙を始めとして極めて広範
囲、多方面にわたっている。
"Prior Art" In recent years, microencapsulation technology has made remarkable progress, and the fields of use of encapsulated products are extremely wide and diverse, including pressure-sensitive copying paper.

マイクロカプセルの製造方法としては、コアセルヘーシ
ョン、法、界面重合法、1n−situ重合法等各種の
方法が知られているが、中でもアミノアルデヒド重縮合
樹脂を壁膜として有するカプセルは耐水性、耐溶剤性等
に優れているため、例えばカルボキシメチルセルロース
の存在下で尿素・ホルムアルデヒド重縮合樹脂壁膜を形
成するカプセル化法〔米国特許第3016308号〕実
質的に分散剤を含有しない懸濁液の中で尿素・ホルムア
ルデヒド重縮合樹脂壁膜を形成するカプセル化法〔特公
昭47−28165号〕等、種々の方法が提案されてい
る。しかし、かかるカプセル化法においては、カプセル
芯物質表面への重縮合樹脂の堆積が効率的に成されない
為、希釈水の添加等その調製条件の極めて注意深いコン
トロールが必要である。
Various methods are known for manufacturing microcapsules, such as coacelhesion, interfacial polymerization, and 1n-situ polymerization, but among them, capsules having a wall film made of aminoaldehyde polycondensation resin are water resistant. , excellent solvent resistance, etc., for example, an encapsulation method in which a urea/formaldehyde polycondensation resin wall film is formed in the presence of carboxymethylcellulose [US Pat. No. 3,016,308], a suspension containing substantially no dispersant. Among them, various methods have been proposed, such as an encapsulation method [Japanese Patent Publication No. 47-28165] in which a wall film of a urea/formaldehyde polycondensation resin is formed. However, in such an encapsulation method, since the polycondensation resin is not efficiently deposited on the surface of the capsule core material, extremely careful control of the preparation conditions such as the addition of dilution water is required.

カプセル芯物質表面への重縮合樹脂の堆積を効率化する
ため、例えば分散剤として化学的ないしは物理化学的結
合を行い得る活性基を有する物質を併用する方法〔特公
昭37−12380号〕静電気的な相互作用による相分
離を利用する方法〔特公昭38−12380号、特公昭
48−4717号、特公昭49−18456号〕等が提
案されている。しかしながら、これらの改良方法では、
従来のコンプレックスコアセルベーションを利用したカ
プセル化法と同様に繁雑な工程を必要とするのみならず
、カプセル壁膜中に異質電荷を有する水溶性成分が含有
されるため、乾燥時にカプセル壁膜のヒビ割れを生じる
欠陥が付随する。
In order to improve the efficiency of depositing the polycondensation resin on the surface of the capsule core material, for example, a method of using a substance having an active group capable of chemically or physicochemically bonding as a dispersant [Japanese Patent Publication No. 37-12380] Electrostatic Methods that utilize phase separation due to such interactions [Japanese Patent Publication No. 38-12380, Japanese Patent Publication No. 48-4717, Japanese Patent Publication No. 49-18456] have been proposed. However, with these improvement methods,
Not only does it require a complicated process like the conventional encapsulation method using complex coacervation, but it also contains water-soluble components with different charges in the capsule wall, which causes the capsule wall to dry during drying. It is accompanied by defects that cause cracks.

また、エチレン・無水マレイン酸共重合体やメチルビニ
ルエーテル・無水マレイン酸共重合体等の存在下でメラ
ミンとホルムアルデヒドを重縮合させてアミノアルデヒ
ド樹脂壁膜を有するカプセルを得る方法〔特開昭53−
84881号〕が提案されており、同様の1n−sit
u重合法によるカプセル化法については、例えば特開昭
55−92135号、特開昭56−51238号、特開
昭56−58536号、特開昭56−102934号、
特開昭57−56293号、特開昭58−8689号、
特開昭60−68045号、特開昭60−216838
号、特開昭60−231(140号、特開昭61)1)
38号、特開昭61−25635号、特開昭62−14
51号、特開昭62−19238号等にも各種提案され
ている。
Furthermore, a method for obtaining capsules having an aminoaldehyde resin wall by polycondensing melamine and formaldehyde in the presence of an ethylene/maleic anhydride copolymer, a methyl vinyl ether/maleic anhydride copolymer, etc.
No. 84881] has been proposed, and a similar 1n-sit
Regarding the encapsulation method using the u-polymerization method, for example, JP-A-55-92135, JP-A-56-51238, JP-A-56-58536, JP-A-56-102934,
JP-A-57-56293, JP-A-58-8689,
JP 60-68045, JP 60-216838
No., JP-A-60-231 (No. 140, JP-A-61) 1)
No. 38, JP-A-61-25635, JP-A-62-14
Various proposals have also been made in No. 51, JP-A No. 62-19238, etc.

「発明が解決しようとする問題点」 しかし、このように数多くのカプセル化法が開発提案さ
れているにもかかわらず、これらの方法には次に挙げる
如き短所が付随するため未だ改良の余地が残されている
"Problems to be Solved by the Invention" However, although many encapsulation methods have been developed and proposed, these methods still have the following disadvantages, so there is still room for improvement. left behind.

■ 感圧複写紙で使用される無色の塩基染料をカプセル
芯物質として用いた場合に、無色染料が着色してしまう
ことがある。
■ When a colorless basic dye used in pressure-sensitive copying paper is used as a capsule core material, the colorless dye may become colored.

■ アミノアルデヒド樹脂のカプセル芯物質表面への堆
積が充分に行なわれず、耐熱性、耐湿性、耐溶剤性等に
劣ったカプセルとなってしまうことがある。
(2) The aminoaldehyde resin may not be sufficiently deposited on the surface of the capsule core material, resulting in capsules with poor heat resistance, moisture resistance, solvent resistance, etc.

■ アニオン性の水溶性高分子物質の乳化能及び乳化安
定性が不充分な時は、数百μmの巨大カプセルが生成さ
れたり、系中に未カプセル化芯物質が残ることがある。
(2) When the emulsifying ability and emulsifying stability of anionic water-soluble polymeric substances are insufficient, giant capsules of several hundred μm may be formed or unencapsulated core substances may remain in the system.

■ アニオン性の水溶性高分子物質を製造する際に、モ
ノマー組成によっては高濃度水溶液を調製できず、輸送
コストや溶解に要するエネルギーコストの増大を来すこ
とがある。
(2) When producing anionic water-soluble polymer substances, it may not be possible to prepare a highly concentrated aqueous solution depending on the monomer composition, resulting in increased transportation costs and energy costs required for dissolution.

本発明の目的は、アニオン性の水溶性高分子物質を溶解
した親水性液体中に疎水性液体を乳化分散させてカプセ
ル化する1n−situ重合法における上記の如き問題
点を改良し、優れた特性を有するマイクロカプセルを効
率よく製造する方法を提供することである。
The purpose of the present invention is to improve the above-mentioned problems in the 1n-situ polymerization method in which a hydrophobic liquid is emulsified and dispersed in a hydrophilic liquid containing an anionic water-soluble polymer substance and encapsulated. An object of the present invention is to provide a method for efficiently producing microcapsules having specific properties.

「問題を解決するための手段」 本発明はビニルスルホン酸と芳香族ビニル化合物を構成
モノマーとして含有するアニオン性高分子共重合体の存
在下、アミノアルデヒド樹脂初期縮合物を重縮合させて
疎水性芯物質表面を包被することを特徴とするマイクロ
カプセルの製造方法である。
"Means for Solving the Problem" The present invention involves polycondensing an initial condensate of aminoaldehyde resin in the presence of an anionic polymer copolymer containing vinyl sulfonic acid and an aromatic vinyl compound as constituent monomers to form a hydrophobic material. This is a method for producing microcapsules characterized by enveloping the surface of a core substance.

「作用」 本発明において用いられる上記アニオン性高分子共重合
体の構成子ツマ−である芳香族ビニル化合物とは、芳香
族環にビニル基が導入された化合物であり、具体的には
スチレン、ビニルトルエン、α−メチルスチレン、イソ
プロペニルトルエン等の核アルキル置換α−アルキルス
チレン、β−ブロムスチレン、ビニルナフタレン等が例
示される。
"Function" The aromatic vinyl compound, which is a component of the anionic polymer copolymer used in the present invention, is a compound in which a vinyl group is introduced into an aromatic ring, and specifically, styrene, Nuclear alkyl-substituted α-alkylstyrenes such as vinyltoluene, α-methylstyrene and isopropenyltoluene, β-bromostyrene, and vinylnaphthalene are exemplified.

これらの中でも、特にスチレン或いはビニルトルエンが
好ましく用いられる。
Among these, styrene or vinyltoluene is particularly preferably used.

本発明のアニオン性高分子共重合体はビニルスルホン酸
と芳香族ビニル化合物を必須の構成モノマーとして含有
するが、共重合体製造における重合の進行を容易に行う
ため、またカプセル品質等に応じて各種の疎水性モノマ
ーや親木性モノマーを含有させることが好ましく、具体
的にはエチレン、プロピレン、(メタ)アクリル酸アル
キル、(メタ)アクリル酸ヒドロキシアルキル、アクリ
ロニトリル、酢酸ビニル、アクリルアミド、ターシャリ
ブチルアクリルアミドスルホン酸、スルホエチルメタク
リレート、アリルスルホン酸、メタリルスルホン酸、ビ
ニルベンゼンスルホン酸、アクリル酸、メタクリル酸、
クロトン酸、無水マレイン酸、イタコン酸等が例示され
る。
The anionic polymer copolymer of the present invention contains vinyl sulfonic acid and an aromatic vinyl compound as essential constituent monomers. It is preferable to contain various hydrophobic monomers and wood-philic monomers, specifically ethylene, propylene, alkyl (meth)acrylates, hydroxyalkyl (meth)acrylates, acrylonitrile, vinyl acetate, acrylamide, and tertiary butyl. Acrylamide sulfonic acid, sulfoethyl methacrylate, allyl sulfonic acid, methallyl sulfonic acid, vinylbenzenesulfonic acid, acrylic acid, methacrylic acid,
Examples include crotonic acid, maleic anhydride, and itaconic acid.

なかでもアクリル酸及び/又は(メタ)アクリル酸アル
キルを含有させると芯物質保持性に優れたカプセルが得
られ〔前記(メタ)アクリル酸アルキルのアルキル基は
炭素数1〜8が好ましい〕、特にアクリル酸と(メタ)
アクリル酸アルキルの両方を含有させた場合に優れたカ
プセルが得られる。
Among them, when acrylic acid and/or alkyl (meth)acrylate is contained, capsules with excellent core material retention properties can be obtained [the alkyl group of the alkyl (meth)acrylate preferably has 1 to 8 carbon atoms], and especially Acrylic acid and (meth)
Excellent capsules are obtained when both alkyl acrylates are included.

本発明で用いられる前記特定の共重合体において、ビニ
ルスルホン酸の含有量が少ないとカプセル分散液の粘度
上昇を抑制する効果が充分得られず、多いと乳化安定性
を損なうため、5〜98モル%、好ましくは10〜80
モル%、より好ましくは10〜40モル%程度含有せし
められる。また芳香族ビニル化合物の含有量が少ないと
充分な乳化安定性を付与する効果が得られず、多いと共
重合体の水溶性が悪くなり、又充分なカプセル強度が得
られないため、0.05〜20モル%、好ましくは0.
1〜10モル%、より好ましくは1〜8モル%程度含有
せしめられる。更に上記以外の構成モノマーは0〜95
モル%、好ましくは5〜90モル%、より好ましくは5
0〜85モル%程度の範囲で含有させるのが望ましい。
In the specific copolymer used in the present invention, if the content of vinyl sulfonic acid is small, the effect of suppressing the increase in viscosity of the capsule dispersion liquid cannot be sufficiently obtained, and if the content is too large, the emulsion stability will be impaired. Mol%, preferably 10-80
The content is preferably about 10 to 40 mol%. Furthermore, if the content of the aromatic vinyl compound is too low, the effect of imparting sufficient emulsion stability cannot be obtained, and if the content is too high, the water solubility of the copolymer becomes poor, and sufficient capsule strength cannot be obtained. 05-20 mol%, preferably 0.05 to 20 mol%.
It is contained in an amount of about 1 to 10 mol%, more preferably about 1 to 8 mol%. Furthermore, the constituent monomers other than the above are 0 to 95
mol%, preferably 5 to 90 mol%, more preferably 5
It is desirable to contain it in a range of about 0 to 85 mol%.

かくして得られた特定の共重合体は、水酸化ナトリウム
、水酸化カリウム、炭酸ナトリウム等のアルカリや酢酸
、シュウ酸、塩酸等の酸でpH3〜6の領域の水溶液又
は水分散液として使用されるが、20重重量水溶液の粘
度が20〜5000cps (25℃。
The specific copolymer thus obtained is used as an aqueous solution or dispersion in the pH range of 3 to 6 with an alkali such as sodium hydroxide, potassium hydroxide, or sodium carbonate, or an acid such as acetic acid, oxalic acid, or hydrochloric acid. However, the viscosity of a 20 weight aqueous solution is 20 to 5000 cps (at 25°C).

pH2,0)、好ましくは40〜1500cpsとなる
よう調節するのが望ましい。また、親水性液体中への配
合量は、乳化液調製の容易さ及び乳化液の安定性等を考
慮し、0.5%以上、より好ましくは1.0%以上、最
も好ましくは2.0〜6.0%程度の範囲で調節するの
が望ましい。なお、配合量の上限は系の粘度やカプセル
調製装置等により決定されるが、−船釣には20%以下
にとどめられる。
It is desirable to adjust the pH to 2.0), preferably 40 to 1500 cps. In addition, the amount to be added to the hydrophilic liquid is 0.5% or more, more preferably 1.0% or more, and most preferably 2.0% or more, considering ease of emulsion preparation and emulsion stability. It is desirable to adjust it within a range of about 6.0%. The upper limit of the blending amount is determined by the viscosity of the system, the capsule preparation device, etc., but is limited to 20% or less for boat fishing.

本発明において疎水性芯物質表面を包被するために用い
られるアミノアルデヒド樹脂は、例えば尿素、メラミン
等のアミン類とホルムアルデヒド、ゲルタールアルデヒ
ド、フルフラール等のアルデヒド類とを一種以上重縮合
させて得られるが、グリシン、スルファミン酸、メタノ
ール等で変性しても良い。これらはカプセル壁膜の緻密
さから初期縮合物の形態で使用されるのが好ましいがモ
ノマーでもかまわない。
The aminoaldehyde resin used to cover the surface of the hydrophobic core substance in the present invention is obtained by polycondensing one or more types of amines such as urea and melamine with one or more aldehydes such as formaldehyde, geltaraldehyde, and furfural. However, it may also be modified with glycine, sulfamic acid, methanol, etc. These are preferably used in the form of an initial condensate in view of the density of the capsule wall, but monomers may also be used.

中でもメラミンとホルムアルデヒドを主な出発物質とす
るメラミン・ホルムアルデヒド系樹脂あるいはメラミン
と尿素とホルムアルデヒドを主な出発物質とするメラミ
ン・尿素・ホルムアルデヒド系樹脂はカプセル壁膜の均
−性及び物理的強度において優れており、良好な芯物質
保持性を有するカプセルが得られるため本発明において
特に好ましく用いられる。
Among them, melamine-formaldehyde resins whose main starting materials are melamine and formaldehyde, and melamine-urea-formaldehyde resins whose main starting materials are melamine, urea, and formaldehyde are excellent in the uniformity and physical strength of the capsule wall membrane. It is particularly preferably used in the present invention because capsules having good core substance retention properties can be obtained.

カプセル製造系は酸性領域、好ましくはpH3〜6に調
節されて重縮合反応が進められるが、系を加熱すると反
応が促進されるため、60〜95℃程度の温度に加熱す
るのが望ましい。なお、カプセル製造系には必要に応じ
て、カルボキシル基やスルホン基を有する天然あるいは
合成の高分子やドデシルベンゼンスルホン酸のような低
分子界面活性剤を併用することもできるが、その使用量
は本発明の所望の効果を阻害しない範囲にとどめる必要
がある。
The capsule manufacturing system is adjusted to an acidic range, preferably pH 3 to 6, to allow the polycondensation reaction to proceed, but since heating the system accelerates the reaction, it is desirable to heat the system to a temperature of about 60 to 95°C. In addition, if necessary, natural or synthetic polymers having carboxyl groups or sulfonic groups or low-molecular surfactants such as dodecylbenzenesulfonic acid can be used in the capsule manufacturing system, but the amount used is limited. It is necessary to keep the amount within a range that does not inhibit the desired effects of the present invention.

本発明においてマイクロカプセル中に内包される疎水性
芯物質としては、特に限定するものではないが以下の如
き物質が例示される。
In the present invention, the hydrophobic core substance to be encapsulated in the microcapsules is not particularly limited, but the following substances are exemplified.

魚油、ラード油などの如き動物油類、オリーブ油、落花
生油、亜麻仁油、大豆油、ひまし油などの如き植物油類
、石油、ケロシン、キシレン、トルエンなどの如き鉱物
油類、アルキル置換ジフェニールアルカン、アルキル置
換ナフタリン、ビフェニールエタン、サリチル酸メチル
、アジピン酸ジエチル、アジピン酸ジ−n−プロピル、
アジピン酸ジ−n−ブチル、フタル酸ジ−メチル、フタ
ル酸ジエチル、フタル酸ジ−n−プロピル、フタル酸ジ
−n−ブチル、フタル酸ジ−n−オクチルなどの如き合
成油類のように水に不溶性または実質的に水に不溶性の
液体或いは上記合成油に電子供与性発色剤、電子受容性
顕色剤、配位子化合物、有機金属塩等を溶解した溶液、
水に不溶性の金属の酸化物および塩類、セルロースある
いはアスベストの如き繊維様物質、水に不溶性の合成重
合体物質、鉱物類、顔料類、ガラス類、香料類、香味料
類、殺菌組成物類、生理学的組成物類、肥料組成物類、
液晶、示温材料、難燃剤等。これらは2種類以上を併用
してもよい。
Animal oils such as fish oil, lard oil, etc., vegetable oils such as olive oil, peanut oil, linseed oil, soybean oil, castor oil, etc., mineral oils such as petroleum, kerosene, xylene, toluene, etc., alkyl-substituted diphenylalkanes, alkyl-substituted naphthalene, biphenylethane, methyl salicylate, diethyl adipate, di-n-propyl adipate,
Synthetic oils such as di-n-butyl adipate, di-methyl phthalate, diethyl phthalate, di-n-propyl phthalate, di-n-butyl phthalate, di-n-octyl phthalate, etc. A solution in which an electron-donating color former, an electron-accepting color developer, a ligand compound, an organic metal salt, etc. are dissolved in a water-insoluble or substantially water-insoluble liquid or the above-mentioned synthetic oil;
Water-insoluble metal oxides and salts, fibrous materials such as cellulose or asbestos, water-insoluble synthetic polymeric materials, minerals, pigments, glasses, fragrances, flavors, fungicidal compositions, Physiological compositions, fertilizer compositions,
Liquid crystals, temperature indicating materials, flame retardants, etc. Two or more types of these may be used in combination.

かくして本発明の方法によれば、希釈水の添加等カプセ
ル調製条件の注意深いコントロールを要することな(、
単にカプセル形成材料を混合し、簡単な重縮合条件を与
えるのみで重縮合樹脂が効率よ(カプセル芯物質表面に
堆積し、耐熱性、耐湿性、耐溶剤性に優れたカプセルが
形成される。
Thus, the method of the present invention does not require careful control of capsule preparation conditions, such as the addition of dilution water.
By simply mixing the capsule-forming materials and providing simple polycondensation conditions, the polycondensation resin is efficiently deposited on the surface of the capsule core material, forming capsules with excellent heat resistance, moisture resistance, and solvent resistance.

しかも得られるカプセル分散液は低粘度で巨大カプセル
や凝築物の生成が少なく、未カプセル化芯物質の存在も
極めて少ないカプセル分散液が調製される。
In addition, the obtained capsule dispersion has a low viscosity, has little formation of giant capsules or aggregates, and has an extremely small amount of unencapsulated core material.

本発明の方法によって調製されるマイクロカプセルは、
各種の医薬、香料、塗料、農薬、接着剤、液晶、食品、
防錆剤、トナー等をカプセル化するのに適しており、特
に印刷インキや感圧複写紙等の用途に有用である。
The microcapsules prepared by the method of the present invention are
Various pharmaceuticals, fragrances, paints, pesticides, adhesives, liquid crystals, foods,
It is suitable for encapsulating rust preventive agents, toners, etc., and is particularly useful for applications such as printing ink and pressure-sensitive copying paper.

「実施例」 以下に本発明をより具体的に説明するために、感圧複写
紙用のマイクロカプセルを調製する場合の実施例を記載
するが、勿論、本発明はこれらに限定されるものではな
い。なお、例中の「部」及び「%」は特に断らない限り
それぞれ「重量部」及び「重量%」を示す。
"Example" In order to explain the present invention more specifically, examples for preparing microcapsules for pressure-sensitive copying paper will be described below, but the present invention is of course not limited to these. do not have. In addition, "parts" and "%" in the examples indicate "parts by weight" and "% by weight", respectively, unless otherwise specified.

実施例1 ビニルスルホン酸15モル%、スチレン5モル%、アク
リル酸70モル%、アクリル酸エチル10モル%から成
る共重合体の20%水溶液(25℃、p H2゜0、濃
度20%の粘度50cps ) 37.5部に水1)2
.5部を加え、20%NaOH水溶液でpiを4.6に
調節したものをカプセル製造用水性媒体とした。
Example 1 A 20% aqueous solution of a copolymer consisting of 15 mol% vinyl sulfonic acid, 5 mol% styrene, 70 mol% acrylic acid, and 10 mol% ethyl acrylate (25°C, pH 2°0, viscosity at 20% concentration) 50cps) 37.5 parts water 1) 2
.. 5 parts were added and the pi was adjusted to 4.6 with a 20% NaOH aqueous solution, which was used as an aqueous medium for capsule production.

これにクリスタルバイオレットラクトン5部を溶解した
ジイソプロピルナフタレン(商品名:に−1)3,呉羽
化学社製)105部を添加し、平均粒径が5μ−となる
ように乳化分散した後、乳化液の温度を70℃に昇温し
た。
To this was added 105 parts of diisopropylnaphthalene (trade name: Ni-1) 3, manufactured by Kureha Chemical Co., Ltd., in which 5 parts of crystal violet lactone had been dissolved, and after emulsifying and dispersing it so that the average particle size was 5 μ-, the emulsion was The temperature was raised to 70°C.

次に系中にメチル化メチロールメラミン初期縮金物(商
品名:ベッカミンAPM、80%濃度、大日本インキ化
学社製)20部を加え、攪拌を継続しながら系の温度を
70℃で1時間保持した後冷却して乳白色のカプセル分
散液を得た。
Next, 20 parts of methylated methylolmelamine precondensate (trade name: Beckamine APM, 80% concentration, manufactured by Dainippon Ink Chemical Co., Ltd.) was added to the system, and the temperature of the system was maintained at 70°C for 1 hour while stirring was continued. After cooling, a milky white capsule dispersion was obtained.

実施例2 ビニルスルホン酸15モル%、ビニルトルエン5モル%
、アクリル酸75モル%、アクリル酸ブチル5モル%か
ら成る共重合体の20%水溶液(25℃、pH1,8,
20部濃度での粘度130 cps ) 37.5部に
水1)2.5部を加え、20%NaOH水溶液でpHを
4.6に調節したものをカプセル製造用水性媒体とした
Example 2 Vinyl sulfonic acid 15 mol%, vinyltoluene 5 mol%
, a 20% aqueous solution of a copolymer consisting of 75 mol% acrylic acid and 5 mol% butyl acrylate (25°C, pH 1.8,
Viscosity at a concentration of 20 parts: 130 cps) 2.5 parts of water was added to 37.5 parts of water, and the pH was adjusted to 4.6 with a 20% NaOH aqueous solution to prepare an aqueous medium for capsule production.

これにクリスタルバイオレットラクトン5部を溶解した
ジイソプロピルナフタレン(商品名:に−1)3,呉羽
化学社製)105部を添加し、平均粒径が5μmとなる
ように乳化分散した。
To this was added 105 parts of diisopropylnaphthalene (trade name: Ni-1) 3, manufactured by Kureha Chemical Co., Ltd., in which 5 parts of crystal violet lactone was dissolved, and the mixture was emulsified and dispersed so that the average particle size was 5 μm.

次に系中にメラミン・尿素・ホルムアルデヒド系初期縮
合物(商品名:ベッカミンMA−3,70部濃度、大日
本インキ化学社製)20部を加え、攪拌を継続しながら
系の温度を80℃で2時間保持した後冷却して乳白色の
カプセル分散液を得た。
Next, 20 parts of a melamine/urea/formaldehyde-based initial condensate (trade name: Beckamine MA-3, 70 parts concentration, manufactured by Dainippon Ink Chemical Co., Ltd.) was added to the system, and the temperature of the system was raised to 80°C while stirring was continued. After being held for 2 hours, the mixture was cooled to obtain a milky white capsule dispersion.

実施例3 ビニルスルホン酸25モル%、スチレン5モル%、アク
リル酸70モル%から成る共重合体(25℃、pH2,
1,20部濃度での粘度300 cps )を用いた以
外は実施例1と同様にしてカプセル分散液を得た。
Example 3 A copolymer consisting of 25 mol% vinyl sulfonic acid, 5 mol% styrene, and 70 mol% acrylic acid (25°C, pH 2,
A capsule dispersion liquid was obtained in the same manner as in Example 1, except that a solution having a viscosity of 300 cps at a concentration of 1.20 parts was used.

実施例4 ビニルスルホン酸98モル%、スチレン2モル%から成
る共重合体(25℃、I) H2,6,20%濃度での
粘度1)0 cps )を用いた以外は実施例1と同様
にしてカプセル分散液を得た。
Example 4 Same as Example 1 except that a copolymer consisting of 98 mol% vinyl sulfonic acid and 2 mol% styrene (25°C, I) H2, 6, viscosity at 20% concentration 1) 0 cps) was used. A capsule dispersion was obtained.

実施例5 ビニルスルホン酸10モル%、α−メチルスチレン5モ
ル%、アクリル酸75モル%、メタクリル酸1so−プ
ロピル10モル%から成る共重合体(25℃、p H2
,1,20%濃度での粘度90 cps )を用いた以
外は実施例1と同様にしてカプセル分散液を得た。
Example 5 A copolymer (25°C, pH
A capsule dispersion liquid was obtained in the same manner as in Example 1, except that a viscosity of 90 cps at a concentration of 1,20% was used.

比較例1 アクリル酸94モル%、アクリル酸ブチル3モル%、メ
タクリル酸1so−プロピル3モル%から成る共重合体
(25℃、pH1,8,20%濃度での粘度200cp
s )を用いた以外は実施例1と同様にしてカプセル分
散液を得た。
Comparative Example 1 Copolymer consisting of 94 mol% acrylic acid, 3 mol% butyl acrylate, and 3 mol% 1so-propyl methacrylate (viscosity at 25°C, pH 1, 8, 20% concentration: 200 cp)
A capsule dispersion liquid was obtained in the same manner as in Example 1 except that s) was used.

比較例2 アクリル酸80モル%、ビニルスルホン酸20モル%か
ら成る共重合体(25℃、 pH2,2,20%濃度で
の粘度60cps )を用いた以外は実施例1と同様に
してカプセル分散液を得た。
Comparative Example 2 Capsule dispersion was carried out in the same manner as in Example 1, except that a copolymer consisting of 80 mol% acrylic acid and 20 mol% vinylsulfonic acid (viscosity 60 cps at 25°C, pH 2.2, 20% concentration) was used. I got the liquid.

かくして得られたカプセル分散液を濃度35%となるよ
うに稀釈し、ワイヤーバー18番で怒圧複写紙用下用紙
(商品名:KSコピーブライト、神崎製紙社製)CF圃
面上塗布、乾燥した。この用紙及び各カプセル分散液を
用いて以下の性能比較テストを行いその結果を第1表に
記載した。
The capsule dispersion thus obtained was diluted to a concentration of 35%, applied to the CF field using a wire bar No. 18 (product name: KS Copy Bright, manufactured by Kanzaki Paper Co., Ltd.), and dried. did. The following performance comparison tests were conducted using this paper and each capsule dispersion, and the results are listed in Table 1.

〔芯物質保持性〕[Core material retention]

テスト用紙を120℃で5時間処理し、塗布面の発色度
合をマクベス濃度計(フィルタ:ビジュアル)で測定し
た。芯物質保持性が優れている程、塗布面の発色濃度が
低い(数値が小さい)。
The test paper was treated at 120° C. for 5 hours, and the degree of color development on the coated surface was measured using a Macbeth densitometer (filter: Visual). The better the core substance retention, the lower the color density on the coated surface (smaller the numerical value).

〔未カプセル化芯物質〕[Unencapsulated core material]

カプセル分散液を下用紙CF面に塗布乾燥する時に、カ
プセル化されていない疎水性芯物質が存在するとスポッ
ト状の汚れとなって現れるので、15co+X25am
面積上に存在するスポット状汚れの個数を測定した。
When applying the capsule dispersion liquid to the CF surface of the lower paper and drying it, if there is a hydrophobic core substance that is not encapsulated, it will appear as a spot-like stain.
The number of spot-like stains present on the area was measured.

〔巨大カプセル、凝集物〕[Giant capsules, aggregates]

カプセル分散液を200メツシユのスクリーンで処理し
残渣重量の全カプセル重量に対する百分率(%)で示し
た。
The capsule dispersion was processed through a 200 mesh screen and the weight of the residue was expressed as a percentage (%) of the total weight of the capsules.

〔カプセル分散液粘度〕[Capsule dispersion viscosity]

試料を25℃としてB型粘度計60rp…で測定した。 The sample was heated to 25° C. and measured using a B-type viscometer at 60 rpm.

第1表 「効果」 本発明の方法で使用した特定のアニオン性高分子共重合
体は、疎水性と親水性のバランスが良好であり、乳化能
、乳化安定性、カプセル壁膜形成能にも優れているため
、第1表の結果からも明らかなように、未カプセル化芯
物質、巨大カプセル、凝集物の発生が極めて少なく、芯
物質保持性に優れたカプセルが効率良く形成された。ま
た本発明で用いる共重合体は、比較的低粘度においても
乳化能、乳化安定性、カプセル壁膜形成能に優れ、得ら
れるカプセル分散液も低粘度であるため感圧複写紙製造
における高速塗抹適性に優れている。
Table 1 "Effects" The specific anionic polymer copolymer used in the method of the present invention has a good balance between hydrophobicity and hydrophilicity, and has good emulsifying ability, emulsion stability, and capsule wall forming ability. As is clear from the results in Table 1, the generation of unencapsulated core material, giant capsules, and aggregates was extremely small, and capsules with excellent core material retention were efficiently formed. Furthermore, the copolymer used in the present invention has excellent emulsifying ability, emulsion stability, and capsule wall forming ability even at a relatively low viscosity, and the capsule dispersion obtained also has a low viscosity, so it can be used for high-speed coating in the production of pressure-sensitive copying paper. Excellent aptitude.

特許出願人  神崎製紙株式会社Patent applicant: Kanzaki Paper Co., Ltd.

Claims (5)

【特許請求の範囲】[Claims] (1)ビニルスルホン酸と芳香族ビニル化合物を構成モ
ノマーとして含有するアニオン性高分子共重合体の存在
下、アミノアルデヒド樹脂初期縮合物を重縮合させて疎
水性芯物質表面を包被することを特徴とするマイクロカ
プセルの製造方法。
(1) In the presence of an anionic polymer copolymer containing vinyl sulfonic acid and an aromatic vinyl compound as constituent monomers, the initial condensate of aminoaldehyde resin is polycondensed to cover the surface of the hydrophobic core material. Characteristic method for producing microcapsules.
(2)アミノアルデヒド樹脂初期縮合物がメラミン・ホ
ルムアルデヒド系樹脂初期縮合物である特許請求の範囲
第(1)項記載の製造方法。
(2) The manufacturing method according to claim (1), wherein the aminoaldehyde resin initial condensate is a melamine formaldehyde resin initial condensate.
(3)アミノアルデヒド樹脂初期縮合物がメラミン・尿
素・ホルムアルデヒド系樹脂初期縮合物である特許請求
の範囲第(1)項記載の製造方法。
(3) The manufacturing method according to claim (1), wherein the aminoaldehyde resin initial condensate is a melamine/urea/formaldehyde resin initial condensate.
(4)芳香族ビニル化合物がスチレン及びビニルトルエ
ンより選ばれる少なくとも1種類である特許請求の範囲
第(1)項記載の製造方法。
(4) The manufacturing method according to claim (1), wherein the aromatic vinyl compound is at least one type selected from styrene and vinyltoluene.
(5)アニオン性高分子共重合体が構成モノマーとして
更にアクリル酸及び(メタ)アクリル酸アルキルの少な
くとも1種類を含有する特許請求の範囲第(1)項記載
の製造方法。
(5) The production method according to claim (1), wherein the anionic polymer copolymer further contains at least one of acrylic acid and alkyl (meth)acrylate as a constituent monomer.
JP62320900A 1987-12-17 1987-12-17 Microcapsule manufacturing method Expired - Lifetime JPH078334B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62320900A JPH078334B2 (en) 1987-12-17 1987-12-17 Microcapsule manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62320900A JPH078334B2 (en) 1987-12-17 1987-12-17 Microcapsule manufacturing method

Publications (2)

Publication Number Publication Date
JPH01164433A true JPH01164433A (en) 1989-06-28
JPH078334B2 JPH078334B2 (en) 1995-02-01

Family

ID=18126522

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62320900A Expired - Lifetime JPH078334B2 (en) 1987-12-17 1987-12-17 Microcapsule manufacturing method

Country Status (1)

Country Link
JP (1) JPH078334B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06269658A (en) * 1993-03-19 1994-09-27 Nippon Paper Ind Co Ltd Production of microcapsule
US5503781A (en) * 1993-03-17 1996-04-02 Sakura Color Products Corporation Microencapsulation process
JP2000325776A (en) * 1999-03-12 2000-11-28 Sakura Color Prod Corp Powdered microcapsule and production thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5503781A (en) * 1993-03-17 1996-04-02 Sakura Color Products Corporation Microencapsulation process
JPH06269658A (en) * 1993-03-19 1994-09-27 Nippon Paper Ind Co Ltd Production of microcapsule
JP2000325776A (en) * 1999-03-12 2000-11-28 Sakura Color Prod Corp Powdered microcapsule and production thereof
JP4683687B2 (en) * 1999-03-12 2011-05-18 株式会社サクラクレパス Powdered microcapsule and manufacturing method thereof

Also Published As

Publication number Publication date
JPH078334B2 (en) 1995-02-01

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