JPH0248039A - Production of microcapsule - Google Patents
Production of microcapsuleInfo
- Publication number
- JPH0248039A JPH0248039A JP63200639A JP20063988A JPH0248039A JP H0248039 A JPH0248039 A JP H0248039A JP 63200639 A JP63200639 A JP 63200639A JP 20063988 A JP20063988 A JP 20063988A JP H0248039 A JPH0248039 A JP H0248039A
- Authority
- JP
- Japan
- Prior art keywords
- added
- capsule
- initial condensate
- aminoaldehyde
- producing microcapsules
- 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.)
- Pending
Links
- 239000003094 microcapsule Substances 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- 229920001577 copolymer Polymers 0.000 claims abstract description 16
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 15
- 239000005056 polyisocyanate Substances 0.000 claims abstract description 11
- 229920001228 polyisocyanate Polymers 0.000 claims abstract description 11
- 229920000877 Melamine resin Polymers 0.000 claims abstract description 10
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 claims abstract description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 24
- -1 isocyanate compound Chemical class 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 16
- 239000012948 isocyanate Substances 0.000 claims description 11
- 229920006389 polyphenyl polymer Polymers 0.000 claims description 8
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 7
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 8
- ZXHZWRZAWJVPIC-UHFFFAOYSA-N 1,2-diisocyanatonaphthalene Chemical compound C1=CC=CC2=C(N=C=O)C(N=C=O)=CC=C21 ZXHZWRZAWJVPIC-UHFFFAOYSA-N 0.000 abstract description 2
- 244000144992 flock Species 0.000 abstract 2
- 239000002775 capsule Substances 0.000 description 44
- 238000000034 method Methods 0.000 description 22
- 239000011162 core material Substances 0.000 description 19
- 239000006185 dispersion Substances 0.000 description 17
- 229920005989 resin Polymers 0.000 description 12
- 239000011347 resin Substances 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 8
- 238000006068 polycondensation reaction Methods 0.000 description 7
- 238000005538 encapsulation Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000001804 emulsifying effect Effects 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- IAUKWGFWINVWKS-UHFFFAOYSA-N 1,2-di(propan-2-yl)naphthalene Chemical compound C1=CC=CC2=C(C(C)C)C(C(C)C)=CC=C21 IAUKWGFWINVWKS-UHFFFAOYSA-N 0.000 description 2
- YJTKZCDBKVTVBY-UHFFFAOYSA-N 1,3-Diphenylbenzene Chemical group C1=CC=CC=C1C1=CC=CC(C=2C=CC=CC=2)=C1 YJTKZCDBKVTVBY-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- MBHRHUJRKGNOKX-UHFFFAOYSA-N [(4,6-diamino-1,3,5-triazin-2-yl)amino]methanol Chemical class NC1=NC(N)=NC(NCO)=N1 MBHRHUJRKGNOKX-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005354 coacervation Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000000975 dye Substances 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 150000002513 isocyanates Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- 229920003169 water-soluble polymer Polymers 0.000 description 2
- LIZLYZVAYZQVPG-UHFFFAOYSA-N (3-bromo-2-fluorophenyl)methanol Chemical compound OCC1=CC=CC(Br)=C1F LIZLYZVAYZQVPG-UHFFFAOYSA-N 0.000 description 1
- WBIQQQGBSDOWNP-UHFFFAOYSA-N 2-dodecylbenzenesulfonic acid Chemical compound CCCCCCCCCCCCC1=CC=CC=C1S(O)(=O)=O WBIQQQGBSDOWNP-UHFFFAOYSA-N 0.000 description 1
- PYSRRFNXTXNWCD-UHFFFAOYSA-N 3-(2-phenylethenyl)furan-2,5-dione Chemical compound O=C1OC(=O)C(C=CC=2C=CC=CC=2)=C1 PYSRRFNXTXNWCD-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical class CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Natural products NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 description 1
- 239000004471 Glycine Substances 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- 238000012695 Interfacial polymerization Methods 0.000 description 1
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- QORUGOXNWQUALA-UHFFFAOYSA-N N=C=O.N=C=O.N=C=O.C1=CC=C(C(C2=CC=CC=C2)C2=CC=CC=C2)C=C1 Chemical compound N=C=O.N=C=O.N=C=O.C1=CC=C(C(C2=CC=CC=C2)C2=CC=CC=C2)C=C1 QORUGOXNWQUALA-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 241000796522 Olene Species 0.000 description 1
- 229920000147 Styrene maleic anhydride Polymers 0.000 description 1
- 229910008649 Tl2O3 Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000000981 basic dye Substances 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 229940060296 dodecylbenzenesulfonic acid Drugs 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 125000003630 glycyl group Chemical group [H]N([H])C([H])([H])C(*)=O 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- AYLRODJJLADBOB-QMMMGPOBSA-N methyl (2s)-2,6-diisocyanatohexanoate Chemical compound COC(=O)[C@@H](N=C=O)CCCCN=C=O AYLRODJJLADBOB-QMMMGPOBSA-N 0.000 description 1
- XJRBAMWJDBPFIM-UHFFFAOYSA-N methyl vinyl ether Chemical compound COC=C XJRBAMWJDBPFIM-UHFFFAOYSA-N 0.000 description 1
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical group CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 239000001254 oxidized starch Substances 0.000 description 1
- 235000013808 oxidized starch Nutrition 0.000 description 1
- QTQRFJQXXUPYDI-UHFFFAOYSA-N oxo(oxothallanyloxy)thallane Chemical compound O=[Tl]O[Tl]=O QTQRFJQXXUPYDI-UHFFFAOYSA-N 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical class OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 1
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 1
- 229920000172 poly(styrenesulfonic acid) Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229940005642 polystyrene sulfonic acid Drugs 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 229940006186 sodium polystyrene sulfonate Drugs 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 229940100445 wheat starch Drugs 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/06—Making microcapsules or microballoons by phase separation
- B01J13/14—Polymerisation; cross-linking
- B01J13/18—In situ polymerisation with all reactants being present in the same phase
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Color Printing (AREA)
- Manufacturing Of Micro-Capsules (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は、疎水性油性液を内包するマイクロカプセルの
製造方法に関し、特に未カプセル化油性液や巨大カプセ
ルが少なく、かつ耐光性に優れた感圧複写紙が得られる
マイクロ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 producing microcapsules encapsulating a hydrophobic oily liquid, and in particular, a method for producing microcapsules that contain less unencapsulated oily liquid and large capsules and has excellent light resistance. The present invention relates to a method for extremely easily producing microcapsules from which pressure-sensitive copying paper can be obtained.
「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、コアセルベーシ
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4718165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 coacervation, interfacial polymerization, and 1n-situ polymerization, but among them, capsules having a wall film made of aminoaldehyde polycondensation resin are water resistant and resistant. Because of its excellent solvent properties, it can be used, for example, in the encapsulation method of forming a urea/formaldehyde polycondensation resin wall film in the presence of carboxymethyl cellulose [US Pat. Among them, various methods have been proposed, such as an encapsulation method [Japanese Patent Publication No. 4718165] in which a urea/formaldehyde polycondensation resin wall film 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3B−12380号、特公
昭48−4717号、特公昭4918456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Hり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し
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 natural interactions [Japanese Patent Publication No. 3B-12380, Japanese Patent Publication No. 48-4717, Japanese Patent Publication No. 4918456] 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 a water-soluble component with a foreign charge in the capsule wall, which causes the capsule wall to dry during drying. 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in 5i
tu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56100629号、
特開昭56−102934号、特開昭56−10293
5号、特開昭57−56293号、特開昭58−868
9月、特開昭60−68045号、特開昭60−216
838号、特開昭60−238140号、特開昭61−
11138号、特開昭61−25635号、特開昭62
−1451号、゛特開昭62−19238号、特開昭6
2−269742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 in 5i
Regarding the encapsulation method using the tu polymerization method, for example, JP-A-55-92135, JP-A-56-51238, JP-A-56-58536, JP-A-56100629,
JP-A-56-102934, JP-A-56-10293
No. 5, JP-A-57-56293, JP-A-58-868
September, JP-A-60-68045, JP-A-60-216
No. 838, JP-A-60-238140, JP-A-61-
No. 11138, JP-A-61-25635, JP-A-62
-1451, Japanese Patent Publication No. 62-19238, Japanese Patent Publication No. 62-1923
Various proposals have also been made in No. 2-269742 and the like.
[発明が解決しようとする課題」
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
。[Problem to be solved by the invention] However, although many encapsulation methods have been developed and proposed, there is still room for improvement as these methods have the following disadvantages. has been done.
■ 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
積が充分に行われず、耐光性、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 light resistance, 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.
また、アミノアルデヒド樹脂壁nりを有するマイクロカ
プセルの製造において、親水性媒体中にスチレン−無水
マレイン酸共重合体やポリスチレンスルフォン酸を乳化
剤として添加した場合、乳化能と乳化安定性が不十分で
あり、数百μmの巨大カプセルが生成したり、未カプセ
ル化芯物質が残る欠点があった。本発明者等は、乳化剤
としてαメチルスチレン−無水マレイン酸共重合体を用
いることにより、上記の欠点が改善されることを見出し
たが、その効果は必ずしも十分ではなく、感圧複写用中
用紙に仕上げた場合、顕色剤層塗布面にスポット状の発
色汚れが生じてしまう問題があった。Furthermore, in the production of microcapsules having an aminoaldehyde resin wall, when a styrene-maleic anhydride copolymer or polystyrene sulfonic acid is added as an emulsifier to a hydrophilic medium, the emulsifying ability and emulsion stability are insufficient. However, there were disadvantages in that giant capsules of several hundred μm were formed and unencapsulated core material remained. The present inventors have found that the above-mentioned drawbacks can be improved by using α-methylstyrene-maleic anhydride copolymer as an emulsifier, but the effect is not necessarily sufficient, and the inner paper for pressure-sensitive copying When finished, there is a problem in that spot-like colored stains occur on the surface coated with the color developer layer.
本発明は、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アミノアルデ
ヒド系樹脂壁膜を有するマイクロカプセル化法における
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ことを目的とする。The present invention improves the above-mentioned problems in the microencapsulation method in which a hydrophobic liquid is emulsified and dispersed in a hydrophilic liquid in which an anionic water-soluble polymer substance is dissolved, and an aminoaldehyde resin wall film is formed. The purpose is to efficiently produce microcapsules with excellent properties.
1課題を解決すにための手段」
本発明は、α−メチルスチレン−無水マレイン酸共重合
体を含有する親水性媒体中で、アミノ・アルデヒド初期
縮合物を重合させて、疎水性油性液表面を包被するマイ
クロカプセル製造方法において、該疎水性油性液が多価
イソシアネート化合物を含有することを特徴とするマイ
クロカプセル製造方法である。1. Means for Solving the Problems The present invention involves polymerizing an amino-aldehyde initial condensate in a hydrophilic medium containing an α-methylstyrene-maleic anhydride copolymer to form a hydrophobic oily liquid surface. In this method, the hydrophobic oily liquid contains a polyvalent isocyanate compound.
「作用」
親水性媒体中に添加するα−メチルスチレン無水マレイ
ン酸共重合体は公知の方法で製造される。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
の共重合体を溶解する溶剤中で行われたり、ベンゼン、
l・ルエン、キシレンなど共重合体を析出させる溶剤中
で共重合反応を行う。このようにして得られた共重合体
はアンモニア、アルカリ金属の水酸化物、有機アミン等
で加水分解され水溶化される。"Operation" The α-methylstyrene maleic anhydride copolymer to be added to the hydrophilic medium is produced by a known method. For example, it is carried out in a solvent that dissolves the copolymer such as acetone, methyl ethyl ketone, methyl isobutyl ketone, benzene,
A copolymerization reaction is carried out in a solvent that precipitates a copolymer, such as l.luene or xylene. The copolymer thus obtained is hydrolyzed with ammonia, an alkali metal hydroxide, an organic amine, etc. to make it water-soluble.
加水分解率は適宜調節される。α−メチルスチレンと無
水マレイン酸の共重合体を構成するモノマー比は略50
モル%−50モル%程度の組成が好ましい。The hydrolysis rate is adjusted as appropriate. The monomer ratio constituting the copolymer of α-methylstyrene and maleic anhydride is approximately 50
A composition of about mol % to 50 mol % is preferable.
α−メチルスチレン−無水マレイン酸共重合体の親水性
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、一般には
20%以下にとどめられる。The amount of α-methylstyrene-maleic anhydride copolymer to be blended in the hydrophilic liquid is 0.5% or more, more preferably 1.0% or more, taking into account ease of emulsion preparation and stability of the emulsion.
It is desirable to adjust the content to 0% or more, most preferably within a range of about 2.0 to 6.0%. The upper limit of the blending amount is determined by the viscosity of the system, the capsule preparation device, etc., but is generally kept at 20% or less.
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・ホルムアルデヒド初期縮合物あるいはメラ
ミンとゲルタールアルデヒドとホルムアルデヒドを主な
出発物質とするメラミン・グルタールアルデヒド・ホル
ムアルデヒド初期縮合物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, a melamine-formaldehyde initial condensate containing melamine and formaldehyde as the main starting materials, or a melamine-glutaraldehyde-formaldehyde initial condensate containing melamine, geltaraldehyde, and formaldehyde as the main starting materials has a significant effect on the uniformity of the capsule wall membrane. It is particularly preferably used in the present invention because it provides capsules with excellent physical strength and good core material retention.
本発明では、疎水性油性液の中に、微量の多価イソシア
ネート化合物を加えることに特徴を有し、これにより芯
物質の乳化安定性を高めて巨大カプセルの生成を防ぐ効
果が得られる。The present invention is characterized in that a trace amount of a polyvalent isocyanate compound is added to the hydrophobic oily liquid, which has the effect of increasing the emulsion stability of the core substance and preventing the formation of giant capsules.
このような多価イソシアネート化合物としては、例えば
ナフタレンジイソシアネート、トリフェニルメタントリ
イソシアネート、ポリメチレンポリフェニルポリイソシ
ア不一ト、リジンジイソシアネート、単量体イソシアネ
ートと多価アルコールとを反応させたアダクト体のよう
な変性イソシアネートやウレタンプレポリマー等が例示
される。Examples of such polyvalent isocyanate compounds include naphthalene diisocyanate, triphenylmethane triisocyanate, polymethylene polyphenyl polyisocyanate, lysine diisocyanate, and adducts obtained by reacting monomeric isocyanates with polyhydric alcohols. Examples include modified isocyanates and urethane prepolymers.
これらは単独もしくは組合わて用いられるが、芳香族系
と脂肪族系のイソシアネートを組合せて使用すると一層
好ましい。なお、疎水性液体中に添5〜1.5重量部に
とどめるのが望ましい。These may be used alone or in combination, but it is more preferable to use a combination of aromatic and aliphatic isocyanates. Note that it is desirable to limit the amount of the additive to 5 to 1.5 parts by weight in the hydrophobic liquid.
多価イソシアネート化合物の添加量が多いと、乳化に要
する時間が長くなったり、またアミノアルデヒド樹脂壁
膜本来の長所を損なうことにでる。If the amount of the polyvalent isocyanate compound added is large, the time required for emulsification will become longer and the original advantages of the aminoaldehyde resin wall film will be impaired.
また、予想外なことに、多価イソシアネート化合物、と
りわけ下記式で例示されるポリメチレンポリフェニルボ
リイソシア不一トを用いるとカプセルの耐光性が向上す
ることが分かった。Furthermore, unexpectedly, it has been found that the use of a polyvalent isocyanate compound, particularly polymethylene polyphenyl polyisocyanate exemplified by the following formula, improves the light resistance of the capsule.
〔nは0以上の整数を表し、通常はn=0〜9のものや
、その混合物が好ましく用いられる。〕ここで耐光性と
は、塩基性無色染料を含むマイクロカプセル含有層を太
陽光、紫外線ランプ等にさらすことにより生じる発色能
の低下、のことを言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液体としては、例えば綿実油、水素
化ターフェニル、水素化ターフェニル誘導体、アルキル
ビフェニル、アルキルナフタレン、ジアリールアルカン
、灯油、パラフィン、ナフテン油、フタル酸エステルな
どの二塩基酸エステル等が挙げられるが、これらは2種
類以上を併用してもよい。[n represents an integer of 0 or more, and usually n=0 to 9 or a mixture thereof is preferably used. ] Here, light resistance refers to a decrease in coloring ability caused by exposing a microcapsule-containing layer containing a basic colorless dye to sunlight, an ultraviolet lamp, etc. Examples of the liquid include cottonseed oil, hydrogenated terphenyl, hydrogenated terphenyl derivatives, alkyl biphenyl, alkylnaphthalene, diarylalkane, kerosene, paraffin, naphthenic oil, and dibasic acid esters such as phthalate esters. Two or more types of these may be used in combination.
カプセル製造系は酸性領域、好ましくはp113〜6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°C程度の温度に加
熱するのが望ましい。なお、親水性媒体中には必要に応
して、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 p113 to 6, to proceed with the polycondensation reaction, 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 hydrophilic medium, but their use is not recommended. The amount must be kept within a range that does not inhibit the desired effects of the present invention.
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く、
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くカプセル芯物質表面に
堆積し、耐光性、耐熱性、耐湿性、耐溶剤性に優れたカ
プセルが形成される。しかも巨大カプセルや凝集物の生
成がなく、未カプセル化芯物質の存在もないカプセル分
散液が調製される。Thus, the method of the present invention does not require careful control of capsule preparation conditions such as addition of dilution water;
By simply mixing capsule-forming materials and applying simple polycondensation conditions, the polycondensed resin is efficiently deposited on the surface of the capsule core material, forming capsules with excellent light resistance, heat resistance, moisture resistance, and solvent resistance. Ru. Moreover, a capsule dispersion is prepared without the formation of giant capsules or aggregates, and without the presence 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、M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, M medicines, 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J及び1%」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, "part J and 1%" in the examples indicate "part by weight" and "weight %", respectively, unless otherwise specified.
実施例工
α−メチルスチレン−無水マレイン酸共重合体(モル比
50%−50%)加水分解物の35%水溶液(25°C
,pH11,9,粘度400cps) 30部に水17
0部を加え、酢酸でpHを4.5に調節したものをカプ
セル製造用親水性媒体とした。Example 35% aqueous solution of α-methylstyrene-maleic anhydride copolymer (molar ratio 50%-50%) hydrolyzate (25°C
, pH 11.9, viscosity 400 cps) 30 parts water 17
0 parts was added and the pH was adjusted to 4.5 with acetic acid, which was used as a hydrophilic medium for capsule production.
これにクリスタルハイオレントラクト75部を溶解した
ジイソプロピルナフタレン(商品名:に113、呉羽化
学社製)105部にポリメチレンポリフェニルポリイソ
シアネート(商品名二ミリオネート MR400,日本
ポリウレタン工業社製)1部を加えて調製した疎水性芯
物質を加え、平均粒径が5μmとなるよう乳化分散した
。To 105 parts of diisopropyl naphthalene (trade name: Ni-113, manufactured by Kureha Kagaku Co., Ltd.) in which 75 parts of Crystal High Olene Tract was dissolved, 1 part of polymethylene polyphenyl polyisocyanate (trade name: 2 Millionate MR400, manufactured by Nippon Polyurethane Industries, Ltd.) was added. In addition, the prepared hydrophobic core material was added and emulsified and dispersed so that the average particle size was 5 μm.
次にメチル化メチロールメラミン初期縮合物(商品名:
ベッカミン APM、85%濃度、大日本インキ化学社
製)20部を加え、撹拌をW続しながら系の温度を90
°C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, methylated methylolmelamine initial condensate (product name:
Add 20 parts of Beckamine APM, 85% concentration, manufactured by Dainippon Ink Chemical Co., Ltd.) and raise the temperature of the system to 90% while stirring continuously.
After being kept at °C for 1 hour, it was cooled to obtain a milky white capsule dispersion.
実施例2
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105部にヘキサメチレンジイソシ
アネート−アダクト体(商品名;デュラネー)24A−
10帆旭化成工業社製)0.1部を加えて調製した疎水
性芯物質を、前記実施例1と同様の親水性媒体に加え、
平均粒径が5μmとなるよう乳化分散した。Example 2 Hexamethylene diisocyanate adduct (trade name: Duraney) 24A- was added to 105 parts of diisopropylnaphthalene in which 5 parts of crystal violet lactone was dissolved.
A hydrophobic core material prepared by adding 0.1 part of 10 (manufactured by Asahi Kasei Kogyo Co., Ltd.) was added to the same hydrophilic medium as in Example 1,
It was emulsified and dispersed so that the average particle size was 5 μm.
次にメラミン・グルタールアルデヒド・ホルムアルデヒ
ド初朋縮金物(60%濃度)30部を加え、撹拌を継続
しながら系の温度を90’C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, 30 parts of melamine/glutaraldehyde/formaldehyde initial aggregation material (60% concentration) was added, and the temperature of the system was maintained at 90'C for 1 hour while stirring, and then cooled to form a milky white capsule dispersion. Obtained.
実施例3
実施例1と同様の乳化分散液ζこメラミン・グルタール
アルデヒド・ホルムアルデヒド系初期縮合物(70%濃
度)30部を加え、撹拌を継続しながら系の温度を80
℃で2時間保持した徒、冷却して乳白色のカプセル分散
液を得た。Example 3 Add 30 parts of a melamine/glutaraldehyde/formaldehyde initial condensate (70% concentration) to the same emulsified dispersion as in Example 1, and raise the temperature of the system to 80°C while continuing to stir.
After being kept at ℃ for 2 hours, it was cooled to obtain a milky white capsule dispersion.
実施例4
ポリメチレンポリフェニルポリイソシアネートの添加量
を0.1部にした以外は、実施例1と同様にカプセル分
散液を得た。Example 4 A capsule dispersion was obtained in the same manner as in Example 1, except that the amount of polymethylene polyphenyl polyisocyanate added was 0.1 part.
比較例1
メチル化メチロールメラミン初期縮合物を加えなかった
こと以外は実施例1と同様にした。Comparative Example 1 The same procedure as Example 1 was carried out except that the methylated methylolmelamine initial condensate was not added.
比較例2
ポリメチレンポリフェニルポリイソシアネートを加えな
かったこと以外は実施例1と同様にして、カプセル分散
液を得た。Comparative Example 2 A capsule dispersion was obtained in the same manner as in Example 1 except that polymethylene polyphenyl polyisocyanate was not added.
比較例3
α−メチルスチレン・無水マレイン酸共重合体の代わり
に、ポリスチレンスルフオン酸ソーダ(商品名: VE
R5A Tl2O3,ナショナルスターチ社製)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 3 Sodium polystyrene sulfonate (trade name: VE) was used instead of α-methylstyrene/maleic anhydride copolymer.
A capsule dispersion was obtained in the same manner as in Example 1 except that R5A Tl2O3 (manufactured by National Starch) was used.
比較例4
ポリメチレンポリフェニルポリイソシアネートを加えな
かったこと以外は比較例3と同様にしてカプセル分散液
を得た。Comparative Example 4 A capsule dispersion was obtained in the same manner as in Comparative Example 3 except that polymethylene polyphenyl polyisocyanate was not added.
比較例5
α−メチルスチレン・無水マレイン酸共重合体の代わり
に、スチレン・無水マレイン酸共重合体(商品名:スフ
リプセット520.モンサント社製)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 5 Capsules were prepared in the same manner as in Example 1, except that a styrene/maleic anhydride copolymer (trade name: Suflipset 520, manufactured by Monsanto) was used instead of the α-methylstyrene/maleic anhydride copolymer. A dispersion was obtained.
比較例6
ポリメチレンポリフェニルポリイソシアネートを加えな
かったこと以外は比較例5と同様にしてカプセル分散液
を得た。Comparative Example 6 A capsule dispersion was obtained in the same manner as in Comparative Example 5 except that polymethylene polyphenyl polyisocyanate was not added.
かくして得られたカプセル分散液を濃度30%となるよ
うに稀釈し、ワイヤーバー20番で感圧複写紙用下用紙
(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、テスト用紙を得た。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 30%, applied to the CF field using a wire bar No. 20 (product name: KS Copy Bright, manufactured by Kanzaki Paper Co., Ltd.), and dried. and obtained a test paper. Using this paper and each capsule dispersion, we conducted the following performance comparison test.
The results are listed in Table 1.
テスト用紙を120°C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稈、塗布面の発色濃度
が低い(数値が小さい。)〔未カプセル化芯物質〕
15 cmX25 cm面積上に存在するスポット状汚
れの個数を測定した。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). Culm with excellent core material retention, low coloring density on coated surface (small value) [Unencapsulated core material] The number of spot-like stains present on an area of 15 cm x 25 cm was measured.
カプセル分散液を下用紙の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。When coating the capsule dispersion liquid on the CF side of the bottom paper and drying it,
The presence of unencapsulated hydrophobic core material appears as spots.
[巨大カプセル、凝集物]
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。[Giant capsules, aggregates] 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.
また、別に得られたカプセル分散液にそれぞれカプセル
中の芯物質100部に対して小麦デンプン70部、溶解
酸化デンプン20部(固形分)を加え、40 g/m2
の原紙に乾燥重量が4g/m2になるように塗布乾燥し
て感圧複写紙用上用紙を作成した。In addition, 70 parts of wheat starch and 20 parts of dissolved oxidized starch (solid content) were added to each separately obtained capsule dispersion liquid for 100 parts of the core material in the capsule, and 40 g/m2 was added.
A top paper for pressure-sensitive copying paper was prepared by coating and drying the mixture on base paper to a dry weight of 4 g/m2.
上用紙と下用紙を重ね合わせ、100 kg/cm2の
荷重をかけて発色像を形成させ、発色濃度をマクヘス濃
度計(マクベク社製、RD−914型)でビジュアルフ
ィルターを用いて測定し、この時の発色濃度をDoとし
た。The upper paper and the lower paper were overlapped, a color image was formed by applying a load of 100 kg/cm2, and the color density was measured using a visual filter using a MacHess densitometer (Model RD-914, manufactured by MacBec). The color density at the time was set as Do.
上用紙のマイクロカプセル分散液の塗布面に20cmの
距離より紫外線を5時間照射(ナショナル)゛ランクラ
イトフ゛ル−、IOW、FLIOBLB)した後、上記
と同様に下用紙と対向させ、100 kg/cm2の荷
重をかけて発色像を形成させ発色濃度をマクベス濃度計
で測定し、この時の発色濃度をり、とした。After irradiating the surface of the upper paper coated with the microcapsule dispersion liquid with ultraviolet rays from a distance of 20 cm for 5 hours (National Inc.'s Rank Light Filter, IOW, FLIOBLB), it was placed facing the lower paper in the same manner as above, and was heated at 100 kg/cm2. A color image was formed by applying a load of 1, and the color density was measured using a Macbeth densitometer, and the color density at this time was defined as .
上記の発色濃度から耐光性を次のごとく規定した。〔数
値が100に近い程耐光性が良好〕L
耐光性−×100
第1表
「効果」
本発明のマイクロカプセルは、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
物の発生がなく、芯物質保持性に優れたカプセルが効率
よく形成された。Light resistance was defined as follows from the above color density. [The closer the number is to 100, the better the light resistance] L Light resistance - x 100 Table 1 "Effects" As is clear from the results in Table 1, the microcapsules of the present invention have a large Capsules with excellent core material retention properties were efficiently formed without the generation of capsules or aggregates.
また本発明は耐光性に優れた感圧複写紙用マイクロカプ
セルの製造方法であった。The present invention also provides a method for producing microcapsules for pressure-sensitive copying paper that have excellent light resistance.
Claims (5)
含有する親水性媒体中で、アミノアルデヒド初期縮合物
を重合させて、疎水性油性液表面を包被するマイクロカ
プセル製造方法において、該疎水性油性液が多価イソシ
アネート化合物を含有することを特徴とするマイクロカ
プセル製造方法。(1) A method for producing microcapsules in which an aminoaldehyde initial condensate is polymerized in a hydrophilic medium containing an α-methylstyrene-maleic anhydride copolymer to cover the surface of a hydrophobic oily liquid. A method for producing microcapsules, characterized in that the oily liquid contains a polyvalent isocyanate compound.
アルデヒド初期縮合物である請求項第(1)記載のマイ
クロカプセル製造方法。(2) The method for producing microcapsules according to claim (1), wherein the aminoaldehyde initial condensate is a melamine formaldehyde initial condensate.
ールアルデヒド・ホルムアルデヒド初期縮合物である請
求項第(1)記載のマイクロカプセル製造方法。(3) The method for producing microcapsules according to claim 1, wherein the aminoaldehyde initial condensate is a melamine/glutaraldehyde/formaldehyde initial condensate.
ェニルポリイソシアネートである請求項第(1)記載の
マイクロカプセル製造方法。(4) The method for producing microcapsules according to claim (1), wherein the polyvalent isocyanate compound is polymethylene polyphenyl polyisocyanate.
液100重量部に対し、0.05〜1.5重量部である
請求項第(1)記載のマイクロカプセル製造方法。(5) The method for producing microcapsules according to claim 1, wherein the amount of the polyvalent isocyanate compound added is 0.05 to 1.5 parts by weight per 100 parts by weight of the hydrophobic oily liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63200639A JPH0248039A (en) | 1988-08-10 | 1988-08-10 | Production of microcapsule |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63200639A JPH0248039A (en) | 1988-08-10 | 1988-08-10 | Production of microcapsule |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0248039A true JPH0248039A (en) | 1990-02-16 |
Family
ID=16427737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63200639A Pending JPH0248039A (en) | 1988-08-10 | 1988-08-10 | Production of microcapsule |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0248039A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000325776A (en) * | 1999-03-12 | 2000-11-28 | Sakura Color Prod Corp | Powdered microcapsule and production thereof |
JP2000342956A (en) * | 1999-04-01 | 2000-12-12 | Dai Ichi Kogyo Seiyaku Co Ltd | Microcapsule production method and microcapsule obtained thereby |
WO2019181668A1 (en) * | 2018-03-23 | 2019-09-26 | 富士フイルム株式会社 | Microcapsule-containing composition, laundry composition, daycare composition and haircare composition |
-
1988
- 1988-08-10 JP JP63200639A patent/JPH0248039A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
JP2000342956A (en) * | 1999-04-01 | 2000-12-12 | Dai Ichi Kogyo Seiyaku Co Ltd | Microcapsule production method and microcapsule obtained thereby |
WO2019181668A1 (en) * | 2018-03-23 | 2019-09-26 | 富士フイルム株式会社 | Microcapsule-containing composition, laundry composition, daycare composition and haircare composition |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4409156A (en) | Process for producing microcapsules | |
KR880002539B1 (en) | Process for producing microcapsules and microcapsule slurry | |
US4328119A (en) | Method of making microcapsules | |
AU600140B2 (en) | Polyurea and polyurea-epoxy microcapsules | |
US4219604A (en) | Method of forming microcapsules, microcapsular dispersion, and pressure sensitive recording sheet | |
JP2002205458A (en) | Microcapsule having polyurea wall | |
JP2002233749A (en) | Microcapsule with polyurea wall | |
JPS62129141A (en) | Preparation of microcapsule | |
JP2634836B2 (en) | Manufacturing method of microcapsules | |
KR840001591B1 (en) | Process of preparing microcapsule for pressure-sensitive recording paper | |
US4209188A (en) | Microcapsules, method of making same, and carbonless copying system including said microcapsules | |
JPH0248039A (en) | Production of microcapsule | |
JPH028774B2 (en) | ||
JPS60238140A (en) | Preparation of microcapsule | |
JP2534691B2 (en) | Method for producing high-density microcapsules | |
JP2675594B2 (en) | Emulsifier for producing microcapsule, microcapsule using the emulsifier, method for producing the same, and carbon-free pressure-sensitive copying paper using the microcapsule | |
JP2639495B2 (en) | Manufacturing method of microcapsules | |
JPH07275689A (en) | Production of microcapsule | |
JPH078334B2 (en) | Microcapsule manufacturing method | |
JPH01130727A (en) | Production of microcapsule | |
KR910004435B1 (en) | Manufacturing method of microcapsule for pressure-sensitive recording paper | |
JP2543531B2 (en) | Microcapsule manufacturing method | |
JP2649796B2 (en) | Method for producing sustained-release microcapsules | |
JP2981498B2 (en) | Emulsifier for microcapsule, microcapsule using the emulsifier, method for producing the same, and carbonless pressure-sensitive copying paper using the microcapsule | |
JP2865311B2 (en) | Emulsifier for microcapsule, microcapsule using the emulsifier, method for producing the same, and carbonless pressure-sensitive copying paper using the microcapsule |