CN1088849A - The preparation method of microcapsule foamer - Google Patents
The preparation method of microcapsule foamer Download PDFInfo
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- CN1088849A CN1088849A CN 93107289 CN93107289A CN1088849A CN 1088849 A CN1088849 A CN 1088849A CN 93107289 CN93107289 CN 93107289 CN 93107289 A CN93107289 A CN 93107289A CN 1088849 A CN1088849 A CN 1088849A
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Abstract
A kind of alkaline process prepares the technology of microcapsule foamer, the water that the oil phase of compositions such as monomer vinylidene chloride, acrylonitrile and blowing agent and composite suspension agent, alkaline conditioner, water are formed mixes dispersion in proportion, and at 45-80 ℃ of reaction polymerization encystation more than 12 hours down.Product is through separating, washing, and handle with the AEO solution impregnation, the microcapsule foamer that gets white dispersiveness and have good stability after the drying, 11 microns of average grain diameters, be heated to 125 ℃ of volumetric expansions and reach more than 27 times, in order to the preparation foamed resin composition, dispersiveness and serviceability are good, storage at normal temperature half a year, it is stable that quality keeps.
Description
The present invention relates to the microcapsules synthetic method, particularly a kind of technology of alkaline process system microcapsule foamer.
Before the present invention makes, preparation method about microcapsule foamer in the prior art had some reports, as once introducing the aqueous copolymers solution suspension system that to use acid medium and adipic acid that waits the gram molecule ratio and diethanol amine to form among the United States Patent (USP) U.S.P 3615972, there is suitable difficulty in this in production control, often make the product quality of different batches inconsistent.United States Patent (USP) U.S.P 4016110 introduces and adopts the cataloid suspending agent that suspends in water, and add the adipic acid of gram-molecular weights such as citric acid replaces and the copolymer of diethanol amine, can make constant product quality, make the blowing agent product quality basically identical of different batches.Above-mentioned two kinds of methods all adopt the acid reaction condition, acidic materials add uniformity and the dispersibility that affiliation reduces the stability of suspending agent silica and influences microcapsule foamer.And, under acid condition, carry out polymerisation, often cause the decomposition of some monomer such as vinylidene chloride, the microcapsule foamer product of formation is than highly acid (PH＜4), the foamed resin composition bin stability of this highly acid microcapsule foamer preparation is low, and influences serviceability.
The purpose of this invention is to provide a kind of simple and microcapsule foamer preparation method of being easy to control, the destabilizing factor that adopts alkaline polymerization condition and composite suspension agent to be produced with the acid reaction condition that overcomes prior art, thus the foamed resin composition stability that the microcapsule foamer made by this law is prepared is improved with serviceability.
The present invention is such realization: the reactant oil phase is made up of with monomer vinylidene chloride, acrylonitrile and the 3rd monomer such as methacrylic acid low carbon number Arrcostab, acrylic acid low carbon number Arrcostab vinyl acetate etc. blowing agents such as low-boiling point liquid such as saturated hydrocarbons, fluorochloromethane, chlorofluoroethanes, also can add micro-cross-linking monomer such as divinylbenzene, and use oil-soluble initiator.Water is then formed composite suspension agent with cataloid and water-soluble resin such as gelatin, cellulose ether, polyvinyl alcohol, polyacrylic acid sodium salt etc., as alkaline conditioner, each set of dispense of aqueous phase is as follows than (percentage by weight): cataloid 5-10%, alkaline conditioner 15-25%, water-soluble resin 0.3-0.8%, water 60-80% with carbonate, phosphate, borate and their hydroxide etc. of sodium, potassium, ammonia.Above-mentioned oil phase and water are in 1: (the best is 1 to the 3-6 ratio: 3.5-4.5) mix in the band stirred reactor of crossing through nitrogen purge, this moment system PH＞7, the best is PH=7-10, evenly disperse stable droplet then into about 10 microns, reaction is more than 12 hours down 45-80 ℃ (the best is 45-60 ℃), and cooling and centrifugation are washed with water to PH=7, added 1-3% AEO solution impregnation again 8-12 hour, dry, sieve to such an extent that white powder is a microcapsule foamer.The reaction mechanism of this building-up process is: in the suspension system that forms, the drop of each suspension is realized the parcel of microcapsules in the mode of solution precipitation polymers.The process of this microencapsulation can be described as four-stage: the formation of the suspension system that (1) is stable, and water and oil phase mix mutually, and under strong shearing force effect, oil phase is dispersed into and is the about 10 microns stable droplet of diameter.(2) polymerisation initial stage-solution precipitation polymerization begins, when temperature rises to the decomposition temperature of initator, decompose to produce the polymerization of free radical trigger monomer, when macromolecular chain increases in to a certain degree, precipitate and separate out owing to polymer is insoluble to blowing agent, this is the process of solution precipitation polymerization.(3) polymerisation mid-term-microcapsules epithelium stage of growth.Carrying out along with polymerisation, macromolecular chain constantly precipitates from solution separates out, the macromolecular chain that is precipitated out is wound in a ball of string mutually, under stirring action, each dispersed drop produces strong rotation, action of centrifugal force makes a ball of string to the drop surface precipitation, and is bonding mutually, progressively forms the epithelium of one deck capsule.Blowing agent is then because the single core capsule of median plane formation that is gathered in capsule is progressively shunk in capillary effect.(4) polymerization reaction late stage-capsule forms.Along with chain shifts and chain termination, the epithelium of thickness progressively thickens, and the intensity increase becomes tough and tensile solid-state, generates microcapsules.
Adopt method of the present invention can prepare the microcapsules of the monokaryon particle of polymolecularity, do not produce and on the wall of reactor and agitator, almost have bur, 11 microns of the microcapsule foamer average grain diameters of making, PH=6 is near neutral.When being heated to 125 ℃, its volumetric expansion reaches 27 times, stores after 1 year, and its PH is still greater than 5, and foam performance is constant.With the foamed resin composition of the microcapsule foamer preparation of the present invention preparation, outward appearance evenly, good dispersion, storage at normal temperature half a year, its good fluidity, steady quality.
Embodiment:
Press surface compositions preparation oil phase and water earlier.
Oil phase (percentage by weight) %
Vinylidene chloride 47.5
Acrylonitrile 20
Methyl acrylate 11
Pentane 20
Peroxidating carbonic acid diisopropyl ester 0.5
Amount to 100
Water (heavy percentage) %
Borax 22.2
Cataloid 8.9
Polyvinyl alcohol 0.7
Water 68.2
In the stainless steel reactor that the band through nitrogen purge stirs, add 100 parts of oil phases, 450 parts of waters, logical nitrogen is to 0.5MPa, and dispersed with stirring becomes the stable droplet of 10 microns of average diameters, this moment PH＞7, reacted 16 hours cooling then, release down at 55 ℃, centrifugation is washed to PH=7 with clear water.Add 1% AEO solution impregnation at last and do the surface and handled 8 hours, drying and screening gets 80 parts of the microcapsule foamers of white favorable dispersibility.
Description of drawings: earlier monomer, initator and blowing agent are hybridly prepared into oil phase, suspending agent, alkaline conditioner and water are mixed into water, again oil phase and water are added mixing dispersion, polymerization encystation again in the polymerization reaction kettle in proportion.Centrifugation then, product is 7 through being washed to PH, adds poly alkyl alcohol ethylene oxide surface treatment (dipping) 8-12 hour again, drying and screening obtains the microcapsule foamer finished product.
Claims (5)
1, a kind of preparation method of microcapsule foamer, the reactant oil phase is by low-boiling point liquid such as saturated hydrocarbons, fluorochloromethane, blowing agent and monomer vinylidene chlorides such as chlorofluoroethane, acrylonitrile and the 3rd monomer such as methacrylic acid low carbon number Arrcostab, acrylic acid low carbon number Arrcostab, compositions such as vinyl acetate, also can add micro-cross-linking monomer such as divinylbenzene, and use oil-soluble initiator, it is characterized in that forming composite suspension agent with cataloid and water-soluble resin, and make and be reflected under the alkali condition (PH＞7) and carry out, reactants water phase composition (percentage by weight) is: 30% cataloid 5-10%, 0.1N alkaline conditioner 15-25%, water-soluble resin 0.3-0.8%, water 60-80%.Oil phase and water are by 1: 3-6 (weight ratio) is mixed in the reactor that nitrogen purge is crossed, and evenly disperses to react more than 12 hours down at 45-80 ℃ then into about 10 microns drops.
2, method according to claim 1 is characterized in that water-soluble resin is gelatin, cellulose ether, polyvinyl alcohol or polyacrylic acid sodium salt.
3, method according to claim 1 and 2 is characterized in that alkaline conditioner is carbonate, phosphate, borate and their hydroxide of sodium, potassium or ammonia.
4, method according to claim 1 is characterized in that reaction system PH is 7-10.
5, method according to claim 1 is characterized in that soaking 8-12 hour clearly with 1-3% poly alkyl alcohol ethylene oxide ethereal solution after the product washing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93107289A CN1048191C (en) | 1993-06-18 | 1993-06-18 | Method for preparing microcapsule foamer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93107289A CN1048191C (en) | 1993-06-18 | 1993-06-18 | Method for preparing microcapsule foamer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1088849A true CN1088849A (en) | 1994-07-06 |
| CN1048191C CN1048191C (en) | 2000-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN93107289A Expired - Fee Related CN1048191C (en) | 1993-06-18 | 1993-06-18 | Method for preparing microcapsule foamer |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102775550A (en) * | 2012-07-12 | 2012-11-14 | 西能化工科技(上海)有限公司 | Medium-high temperature thermal expansibility microsphere and method for reducing residual monomers therein |
| CN103534304A (en) * | 2011-05-17 | 2014-01-22 | 栗村化学株式会社 | Composition for a starch container, starch container using same, and method for manufacturing the starch container |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1309765C (en) * | 2005-10-20 | 2007-04-11 | 北京科技大学 | Method for preparing porous aquagel using wave polymerisation of microcapsule foaming agent |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3615972A (en) * | 1967-04-28 | 1971-10-26 | Dow Chemical Co | Expansible thermoplastic polymer particles containing volatile fluid foaming agent and method of foaming the same |
| US3740359A (en) * | 1972-07-10 | 1973-06-19 | Dow Chemical Co | Vinylidene chloride expandable microspheres |
| US4016110A (en) * | 1972-07-26 | 1977-04-05 | The Dow Chemical Company | Process for the preparation of expandable microspheres |
| JPS62286534A (en) * | 1986-06-04 | 1987-12-12 | Matsumoto Yushi Seiyaku Kk | Manufacture of thermal expansion microcapsule |
-
1993
- 1993-06-18 CN CN93107289A patent/CN1048191C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103534304A (en) * | 2011-05-17 | 2014-01-22 | 栗村化学株式会社 | Composition for a starch container, starch container using same, and method for manufacturing the starch container |
| US9410032B2 (en) | 2011-05-17 | 2016-08-09 | Youl Chon Chemical Co., Ltd. | Composition for a starch container, starch container using same, and method for manufacturing the starch container |
| CN103534304B (en) * | 2011-05-17 | 2016-10-05 | 栗村化学株式会社 | For the compositions of starch bowl, the starch bowl using said composition and the method manufacturing this starch bowl |
| CN102775550A (en) * | 2012-07-12 | 2012-11-14 | 西能化工科技(上海)有限公司 | Medium-high temperature thermal expansibility microsphere and method for reducing residual monomers therein |
| CN102775550B (en) * | 2012-07-12 | 2014-09-10 | 西能化工科技(上海)有限公司 | Medium-high temperature thermal expansibility microsphere and method for reducing residual monomers therein |
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| Publication number | Publication date |
|---|---|
| CN1048191C (en) | 2000-01-12 |
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