Method of producing microcapsules
专利摘要:
An improved encapsulation process to prepare encapsulated water-immiscible material employing an organic polyisocyanate intermediate to form discrete polyurea capsule enclosures around a water-immiscible material dispersed in an aqueous continuous phase said improvement comprising the addition of a catalytic amount of a phase transfer catalyst. 公开号:SU1022651A3 申请号:SU782625405 申请日:1978-05-31 公开日:1983-06-07 发明作者:Бенсон Шер Герберт 申请人:Стауффер Кемикал Компани (Фирма); IPC主号:
专利说明:
about | tnoshnits to receiving the Invention use, on which microcapsules, tanks for an example, in (herbicides, pesticides contents. item.). insecticides and micro preparations; Organic capsules are known for dispersing a phase consisting of a water-immiscible pesticide or a mixture thereof. polyisoorganic antidote, mash-tertiary cyanate and rolled phase, containing amine into protective colloid, emulsifier and at pH 4.3-5.8 I by polycondensation of hydroxy1roxy sodium in the presence of pH 7-10; the microcapsule is large, the invention is not enough - the intrinsic purpose of the process. This goal is achieved through the preparation of a micronucleus according to the organic dispersion of a capsule phase consisting of a water-immiscible pesticide or a mixture of it with an analogue of the polyisocyanate, the organic matter in the aqueous phase, the soybean catalyst, the torus and the protective ring holding the emulsifier, at pH 4 -5.8 and polycondensation in the presence of sodium hydroxide at pH 7O, as a cate is a cozy tricaprylmelizator. using thylammonium chloride or tri-n-butyl-n-cetylphosphonium chloride. . Water (279 g), with P r and m er holding,%: not; 1ralized polyfirme (maleic an methylvinyl: hydride) 2.0; by. shvinilny alcohol (air defense 0.22 and an alcohol-based emulsifier (tergitol ethoxylated 15-5-7) 0.3, the promotional vessel is placed in an open p using hydrocopper with a pH of 4.3. si Na installed: mixed with S-ethyldiisobuti. 1 thiocarbamate (herbicide) 340; N, NI 1-cyclo-dichloroacetam (herbicidal an goes) 14,2; ) 2,3, phases of the ego. The resulting is placed in a floor of the promotional vessel and emulsified with a force of agitator using a stirrer. The particle size of the remaining 5-40 microns. The soft part of the reaction is saturated, stirring without heating, the pH of the medium is 10, by setting about г g of Na hydroxide. About 20% of the wall / and microcaps / After 2 minutes, Δ92, 3% completed the formation of a catalyst, the presence of microcapsules took 3 hours and 2. In the aqueous phase, Example 1 (471.7 g, 90DY) was used to mix a mixture consisting of 170 g-ethyl diisobutylthiocarbamate ; 7.1 g, K-diallyl dichloroacetamide; 7.9 g ARI; 6.45 g of hexamethylenediisocyana (HMDI) and 1.29 g of tricaprylylmethylammonium chloride. The particle size is set in the range of 5-40 μm H 10. After 2 min, the formation of microcapsules in the dispersion was completed by 50%. Continuous mixing increases the degree of completion by more than one eu. The degree of completion of the reaction is determined by the consumption of Na hydroxide. Under the microscope, the formation of well-formed discrete asters is observed. In the aqueous phase (1710 g of water), analogously to example 1, a mixture consisting of 1700 g of 5-ethylhexahydro-1H-azepine-1-carbothioate (herbicide) is added; 92.0 g RARI; 46.0 g TDI and 11.0 g tricaprylylmethylammonium chloride. Microcapsules are obtained after stirring for 20 minutes. Example 4: According to the procedure of Example 1, a mixture consisting of 317 g of 0.0-dimethyl is added to 378 g of water containing%: PES 2.0 and an emulsifier based on ethoxylated linear alcohol 0.3. -O- | nitrophenyl phosphorothioate (insecticide); 19.3 g of RARI, 6.4 g of TDI and 2.1 f of tricaprylylmethylammonium chloride and emulsification at pH 5.8. The particle size is set at 5-40 microns. Smooth stirring for 1 hour and 25 ° C. The final establishment of pH 7.. . PRI me R 5. According to the procedure of Example 1, 509 g of water containing 2.0% PES and 0.3% of an emulsifier based on an ethoxylated linear alcohol are emulsified with 165 g of S-ethyldiisobutylthiocarbamate (herbicide), 7.3 RARI, 6.0 g TDI and 1.0 g tri-N-butyl-N-Cetyl phosphonium bromide (head-transfer catalyst). The particle size of 5-40 microns. After adding sodium hydroxide pH 10. In approximately 6 minutes, the formation of microcapsules occurs by 56.6%. Stirring is continued to reach the desired degree of completion of the reaction, which is determined by the absorption of sodium hydroxide. Example 6. To form microcapsules, interfacial polymerization is carried out, including hydrolysis of the monomeric isocyanate to form an amine, which in turn reacts with another monomeric isocyanate molecule to form a polyurea capsule. Moderate mixing maintains the dispersion of the organic phase in the aqueous phase and, if necessary, is heated.
权利要求:
Claims (1) [1] ΤΏ) METHOD FOR PRODUCING MICROCapsules by dispersing an organic phase consisting of a water-immiscible pesticide or mixture with an antidote, an organic polyisocyanate and a catalyst, in an aqueous phase containing an emulsifier and a protective colloid, at pH 4.3-5.8 and polycondensation in the presence of sodium hydroxide at a pH of 7–10, which is due to the fact that, in order to intensify the process, triacaprylmethylammonium chloride or tri-n-butylH-cetylphosphonium bromide is used as a catalyst. > refers to the receipt of ve tanks for cides (herbicides, • p.). about getting microiz immiscible a or a mixture of it with. mash - in the tertiary phase, the containment colloid, in the indicated way the intensification goal is achieved by that, in the aqueous phase, co. 0, as cat
类似技术:
公开号 | 公开日 | 专利标题 SU1022651A3|1983-06-07|Method of producing microcapsules US4285720A|1981-08-25|Encapsulation process and capsules produced thereby SU707510A3|1979-12-30|Microcapsule producing method JP3848676B2|2006-11-22|Microcapsules containing suspensions of biologically active compounds TW398955B|2000-07-21|Microcapsule compositions, process for the preparation of microcapsule compositions and uses of the microcapsule compositions AU651511B2|1994-07-21|Microcapsules, a process for their preparation and their use CS249110B2|1987-03-12|Method of water non-miscible substance encapsulation US4681806A|1987-07-21|Particles containing releasable fill material and method of making same CA1104882A|1981-07-14|Encapsulation process US4046741A|1977-09-06|Post-treatment of polyurea microcapsules US4876290A|1989-10-24|Microencapsulation by interfacial polyaddition KR19990008105A|1999-01-25|Microcapsules containing suspensions of biologically active substances and sunscreens RU2108036C1|1998-04-10|Microencapsulated herbicidal composition adapted to controlled release of active principle RU96112119A|1998-09-27|MICROCAPSULES CONTAINING SUSPENSIONS OF BIOLOGICALLY ACTIVE COMPOUNDS JPH08252454A|1996-10-01|Microcapsule with wall prepared of reaction product of polyisocyanate/guanidine CN1167338C|2004-09-22|Novel water-in-oil microencapsulation process and microcapsules produced thereby US4900551A|1990-02-13|Method for preventing termites and microencapsulated organophosphorus termite controlling composition CA1245917A|1988-12-06|Process for producing multiple types of microcapsules US4851227A|1989-07-25|Insecticidal composition comprising diazinon and process for the preparation thereof SU523627A3|1976-07-30|The method of producing microcapsules JP3186783B2|2001-07-11|Manufacturing method of microcapsules KR810001880B1|1981-11-20|Process for preparing capsule empoying phase transfer catalysts JPH06106047A|1994-04-19|Preparation of sustained-releasable microcapsule IE20100721A1|2012-05-23|Agrochemical composition and method of forming the same PL101769B1|1979-01-31|A METHOD OF MAKING CAPSULES FOR SUBSTANCES NON MISCIBLE WITH WATER
同族专利:
公开号 | 公开日 PH16196A|1983-07-28| IT1115076B|1986-02-03| JPS53149179A|1978-12-26| DK156989B|1989-10-30| MX5644E|1983-11-25| BE867646A|1978-11-30| FR2392715A1|1978-12-29| BR7803468A|1979-01-02| CH640151A5|1983-12-30| DD137063A5|1979-08-15| PL207239A1|1979-04-23| NZ187429A|1979-11-01| JPS5826969B2|1983-06-06| DK156989C|1990-03-26| IL54804A|1981-07-31| CA1110503A|1981-10-13| CS198299B2|1980-05-30| YU40039B|1985-06-30| ES470373A1|1979-01-01| AU3663978A|1979-12-06| AU514717B2|1981-02-19| HU181952B|1983-11-28| NL7805878A|1978-12-04| IL54804D0|1978-07-31| BG29865A3|1981-02-16| FR2392715B1|1985-01-18| DE2823377C2|1987-05-07| GB1558460A|1980-01-03| DE2823377A1|1978-12-07| RO75293A|1980-11-30| US4140516A|1979-02-20| IT7849597D0|1978-05-30| ZA783016B|1979-05-30| DK241678A|1978-12-01| AR217296A1|1980-03-14| PL128464B1|1984-01-31| YU130378A|1983-01-21|
引用文献:
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申请号 | 申请日 | 专利标题 US05/801,932|US4140516A|1977-05-31|1977-05-31|Encapsulation process employing phase transfer catalysts| 相关专利
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