CN1160398C - High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process - Google Patents
High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process Download PDFInfo
- Publication number
- CN1160398C CN1160398C CNB011400226A CN01140022A CN1160398C CN 1160398 C CN1160398 C CN 1160398C CN B011400226 A CNB011400226 A CN B011400226A CN 01140022 A CN01140022 A CN 01140022A CN 1160398 C CN1160398 C CN 1160398C
- Authority
- CN
- China
- Prior art keywords
- polymer
- precipitation agent
- solution
- polyvinyl
- high molecular
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The present invention belongs to macromolecule processing. The present invention has the following characteristics: firstly, a precipitation agent is added into a macromolecular solution in drops so as to prompt the phase separation of the solution, and uniform liquid beads rich in macromolecules are obtained; secondly, under the protection of another macromolecule which can not be precipitated, the liquid beads are converted into macromolecular uniform microspheres or needle-shaped fine particles by controlling mixing speed and temperature, and protective macromolecules are added during the preparation of the macromolecular solution and the precipitation agent. In addition, solvents for the preparation of the macromolecular solution are formic acid, dimethyl acetamide, etc., water is adopted as the precipitation agent, and the protective macromolecules are polyvinyl alcohol, etc. By the present invention, dozens of macromolecules such as polyamide, polyether ketone, polyvinylidene fluoride, cellulose acetate, etc. are processed into uniform microspheres or needle-shaped fine particles.
Description
The field is a Process Technology of Polymer under the present invention.
Polymer microsphere (containing the natural polymer microballoon) has a wide range of applications.They be used for making fire-retardant, waterproof, reflective, absorb ultraviolet ray or various functional coatings such as infrared rays, radioprotective.Be used for making high-quality ink and photocopy toner.In food, medicine and cosmetic industry, be used as additive.In chemical industry is synthetic, be used as the carrier of catalyzer.In biotechnology and biotechnology, be used as the carrier or the sorbent material of biological substance such as albumen, enzyme, cell etc. again.They can also be used to preparing the chromatographic column carrier of various gas, liquid chromatography.Also can prepare the immune microsphere and the targeted drug that are used for the medical diagnosis treatment.The polymer acicular microparticles then can be received beyond thought effect, as making the reflective coating with directivity, the chromatographic column carrier of high-bulk-density, anisotropic matrix material etc. because the specificity of shape replaces polymer microsphere in application.
Use existing natural polymer, again they are shaped and be microballoon, more existing patent reports have been reported the method for using Mierocrystalline cellulose and derivative manufacturing microballoon as JP11181147A (1999), EP075000A1 (1996), US5064949A (1991) and JP3028241A (1991).WO9119746A (1991) and EP0087786A (1983) have then reported the forming technique of agar and agarose microbeads.CN1105369A (1995) and JP62100534A (1987) have reported the method for making the chitin microballoon.The synthetic macromolecule microballoon generally all in the Polymer Synthesizing process with monomer by making as suspension polymerization, letex polymerization or diffuse-aggregate method.Use existing synthetic macromolecule, it is rare they to be shaped into microballoon again, has only the report (J.Appl.Polym.Sci.45 (1992) 1783 for W.-H.Hou, T.B.Lloyd) of the monodispersed polymeric amide microballoon of 1 example preparation particle diameter.Use the existing macromolecular material polymer acicular microparticles that is shaped, then yet there are no report.Make a general survey of over the forming technique of making polymer microsphere with existing macromolecular material, mainly be the preparation macromolecular solution, with them or sparge in the high temperature gas flow, or carry out water/oil content and loose, or form the liquid pearl and in precipitation bath, solidify, or heat freezing macromolecular solution and make the balling-up of fractionated polymer phase.The microspherulite diameter that first three kind balling-up technology obtains distributes wide; Last a kind of balling-up technology is run into plant issue again, with assurance heating or freezing equably, otherwise also can not obtain the uniform microballoon of particle diameter.Aforementioned single disperse polyamides microballoon, can only carry out in 10 milliliters test tube because evenly freezing fast with the preparation of refrigerated method, can only prepare the microballoon of 0.1 gram at every turn.
The objective of the invention is to propose a method, make the microballoon or the acicular microparticles of uniform granularity with existing synthesized polymer material.We wish that this is a blanket method, can make synthetic macromolecule as much as possible, comprise the microballoon or the acicular microparticles of natural polymer even.
The homogeneity of microballoon, acicular microparticles size, ε defines with dispersion coefficient.ε=σ/d, d is the mean diameter of microballoon in the formula, or the average major diameter of acicular microparticles.σ is the standard deviation of microsphere diameter, or the standard deviation of acicular microparticles major diameter.For microballoon, ε＜0.1 is referred to as mono-dispersion microballoon, and ε=0.1-0.5 is referred to as uniform microsphere.For acicular microparticles, the uniform acicular microparticles of major diameter still can be thought in ε＜1.0.
Principle of the present invention is at first to prepare macromolecular solution, drips precipitation agent then in solution, impels macromolecular solution to be separated, and produces to be rich in polymer and the uniform liquid pearl of size.Under another kind can not sedimentary polymer protection, control stirring velocity and temperature were not collided each other to keep size stability the liquid pearl, and last liquid pearl is converted into homogeneous macromolecular beads or acicular microparticles.The polymer that shields adds when preparation macromolecular solution and precipitation agent.
For sake of convenience, below the polymer of desiring to be processed into microballoon or acicular microparticles is referred to as the polymer first; The polymer that shields is referred to as polymer second; The solvent of polymer first is referred to as the solvent first, and polymer second also is dissolved in the solvent first; With the precipitation agent of polymer first but be again simultaneously that the solvent of polymer second is referred to as solvent second.
The process of shaping homogeneous macromolecular beads is:
(1) preparation polymer first and the mixing macromolecular solution of second in the solvent first.The concentration range of polymer first is the 0.001-0.1 grams per milliliter, and the concentration of polymer second is polymer first 0.1-10 times.This solution called after solution first.
(2) macromolecular solution of preparation polymer second in solvent second.The concentration range of polymer second is the 0.001-0.2 grams per milliliter, solvent second and solvent first complete miscibility.This solution called after solution second.
(3) solution second is under agitation splashed in the solution first, impel the solution first to be separated.At first produce and be rich in the liquid pearl of polymer first, and gradate swollen microsphere into the polymer first.The consumption of solution second is 1-10 a times of solution first, fully is precipitated out to guarantee the polymer first.When dripping solution second, stirring velocity is 5-500 rev/min.Temperature is lower than the boiling point of solvent first and second.
(4) with filtering, centrifugal or sedimentary method is told the swollen microsphere of polymer first.Soak repeatedly and wash with solvent second, constantly change the polymer second of solvent second with flush away solvent first and a small amount of co-precipitation.At this moment swollen microsphere is shunk gradually, obtains polymer (first) microballoon of uniform granularity at last.
The process of the even acicular microparticles of shaping polymer is:
(1) preparation polymer first and the mixing macromolecular solution of second in the solvent first.The concentration range of polymer first is the 0.001-0.1 grams per milliliter.The concentration of polymer second is 0.1-10 times of polymer first.This solution called after solution first.
(2) macromolecular solution of preparation polymer second in solvent second.The concentration range of polymer second is the 0.001-0.2 grams per milliliter.Solvent second and solvent first complete miscibility.This solution called after solution second.
(3) solution second is under agitation splashed in the solution first, impel the solution first to be separated.At first produce and be rich in the liquid pearl of polymer first, and gradate swelling acicular microparticles into the polymer first.The consumption of solution second is 1-10 a times of solution first, fully is precipitated out to guarantee the polymer first.When dripping solution second, stirring velocity is 100-10000 rev/min.Temperature can be near the boiling point of solvent first and second.
(4) with filtering, centrifugal or sedimentary method is separated the swelling acicular microparticles of polymer first.Soak repeatedly and wash with solvent second, constantly change solvent second, with the polymer second of flush away solvent first and a small amount of co-precipitation.At this moment the swelling acicular microparticles shrinks gradually, obtains polymer (first) acicular microparticles of uniform granularity at last.
The present invention has made two groups of polymer microspheres or acicular microparticles.The characteristics of first group of polymer (first) are all to be dissolved in formic acid or acetate or their mixture (solvent first), all are deposited in water (solvent second).This group polymer (first) has polyvinyl formal, polyvinyl butyral acetal, polyvinyl acetate, polyvinyl methyl ketone, polymethylmethacrylate, polyethyl methacrylate, poly-n-propyl methacrylate, Vinalac 5920, polycaprolactam, PA 66, polyureas, urethane, polycarbodiimide, polybenzimidazole Ju quinoxaline, the tricarboxylic acid Mierocrystalline cellulose, rhodia, soluble cotton, chitin or above-mentioned high molecular mixture.The characteristics of second group of polymer (first) are all to be dissolved in dimethyl formamide or N,N-DIMETHYLACETAMIDE or their mixture (solvent first), all are deposited in water (solvent second).This group polymer (first) has chlorosulfonated polyethylene, polyacetylene, polyvinyl formal, polyvinyl butyral acetal, polyvinyl chloride, polyvinylidene chloride, polyvinylidene difluoride (PVDF), polyvinyl methyl ketone, poly-sulphur vinyl fluoride, polyacrylonitrile, polymethacrylonitrile, polyacrolein, poly-two acryloyl methane, poly acrylic anhydride, polymethacrylic acid anhydride, polyoxymethylene, poly-propionic aldehyde, polyacrolein, polyphenylene oxide, polyetherketone, polysulfones, chloromethyl polysulphone, polyethersulfone, polyether sulphone, polycarbonate, polysulfonamides, polyimide, polyetherimide, polybenzoxazole Ju quinoxaline, methylcellulose gum, rhodia, the cyanoethyl rhodia, three cellulose caproates, three sad Mierocrystalline celluloses or above-mentioned high molecular mixture.In addition, also have some multipolymers,, also can be used for making microballoon or acicular microparticles as long as they satisfy corresponding solvent, precipitation agent requirement.The used polymer that shields (second) of the present invention is polyvinyl alcohol, polyacrylamide, polyvinylpyrrolidone, polyoxyethylene glycol or their mixture.
Description of drawings:
Fig. 1: polycaprolactam microballoon.
Fig. 2: polyetherketone acicular microparticles.
Fig. 3: polyvinylidene difluoride (PVDF) microballoon.
Fig. 4: rhodia microballoon.
Embodiment 1: 1000 milliliters of the polyvinyl alcohol formic acid solutions of inserting polycaprolactam that concentration is 0.01 grams per milliliter and 0.01 grams per milliliter in 5000 milliliters there-necked flask.Under agitation drip the polyvinyl alcohol water solution that concentration is 0.04 grams per milliliter, notice during dropping waiting until that the last basic disappearance of caused precipitation can splash into next.Solution occurs permanent muddy when dropping liquid reaches 650 milliliters.Continue to drip, reach 2000 milliliters until the dropping liquid total amount.Stirring velocity is 250 rev/mins during dropping, and temperature is 25 ℃.Stirring is spent the night.Leached microballoon on the 2nd day, water repetitive scrubbing, oven dry at last, yield 60%.Microsphere diameter d=7.63 micron, Fig. 1 is seen in dispersion coefficient ε=0.16.
Embodiment 2: 1000 milliliters of the polyvinyl alcohol dimethylacetamide solutions of inserting polyetherketone that concentration is 0.01 grams per milliliter and 0.02 grams per milliliter in 5000 milliliters there-necked flask.Under agitation drip the polyvinyl alcohol water solution that concentration is 0.02 grams per milliliter, notice during dropping waiting until that the last basic disappearance of caused precipitation can splash into next.Solution becomes turbid when dropping liquid reaches 30 milliliters, and turbidity reaches the highest after 80 milliliters.Continue to drip, reach 2000 milliliters until the dropping liquid total amount.Stirring velocity is 500 rev/mins during dropping, and temperature is 80 ℃.Stirring is spent the night.Leached acicular microparticles on the 2nd day, water repetitive scrubbing, oven dry at last, yield 65%.Particulate major diameter d=19.6 micron, Fig. 2 is seen in dispersion coefficient ε=0.60.
Embodiment 3: 1000 milliliters of the polyvinyl alcohol dimethylacetamide solutions of inserting polyvinylidene difluoride (PVDF) that concentration is 0.04 grams per milliliter and 0.02 grams per milliliter in 5000 milliliters there-necked flask.Under agitation drip the polyvinyl alcohol water solution that concentration is 0.04 grams per milliliter, notice during dropping waiting until that the last basic disappearance of caused precipitation can splash into next.Solution becomes turbid when dropping liquid reaches 2000 milliliters.Continue to drip, reach 3000 milliliters until the dropping liquid total amount.Stirring velocity is 500 rev/mins during dropping, and temperature is 95 ℃.Stirring is spent the night.The 2nd day with whizzer at 3000 rev/mins of following collection microballoon throw outs, and constantly wash oven dry, yield 82% with water.Microsphere diameter d=2.97 micron, Fig. 3 is seen in dispersion coefficient ε=0.23.
Embodiment 4: 1000 milliliters of the polyvinyl alcohol dimethylacetamide solutions of inserting secondary cellulose acetate that concentration is 0.02 grams per milliliter and 0.04 grams per milliliter in 5000 milliliters there-necked flask.Under agitation drip the polyvinyl alcohol water solution that concentration is 0.04 grams per milliliter, notice during dropping waiting until that the last basic disappearance of caused precipitation can splash into next.Solution becomes turbid when dropping liquid reaches 230 milliliters, and is muddy fully when reaching 400 milliliters.Continue to drip, reach 2000 milliliters until the dropping liquid total amount.Stirring velocity is 250 rev/mins during dropping, and temperature is 40 ℃.Stirring is spent the night.Leached microballoon on the 2nd day, water repetitive scrubbing, oven dry, yield 53%.Microsphere diameter d=8.65 micron, Fig. 4 is seen in dispersion coefficient ε=0.25.
Claims (4)
1. the manufacturing process of the polymer microsphere of uniform granularity is characterized in that:
(1) in desire is shaped high molecular solution and precipitation agent, all dissolved a kind of can sedimentary protection polymer, to keep the microballoon size stability: the high molecular concentration range that is shaped in the solution is the 0.001-0.1 grams per milliliter, protect high molecular concentration be the shaping polymer concentration 0.1-10 doubly; The high molecular concentration range of protection is the 0.001-0.2 grams per milliliter in the precipitation agent;
When (2) dripping precipitation agent, stirring velocity is 5-500 rev/min, and temperature is lower than the solvent that is mixed with the form height molecular solution and the boiling point of precipitation agent.
2. the manufacturing process of the polymer acicular microparticles of uniform granularity is characterized in that:
(1) in desire is shaped high molecular solution and precipitation agent, all dissolved a kind of can sedimentary protection polymer, to keep the acicular microparticles size stability: the high molecular concentration range that is shaped in the solution is the 0.001-0.1 grams per milliliter, protect high molecular concentration be the shaping polymer concentration 0.1-10 doubly; The high molecular concentration range of protection is the 0.001-0.2 grams per milliliter in the precipitation agent;
When (2) dripping precipitation agent, stirring velocity is 100-10000 rev/min, and temperature can approach to be mixed with the solvent of form height molecular solution and the boiling point of precipitation agent.
3. the uniform microsphere and the acicular microparticles of polyvinyl formal, polyvinyl butyral acetal, polyvinyl acetate, polyvinyl methyl ketone, polymethylmethacrylate, polyethyl methacrylate, poly-n-propyl methacrylate, Vinalac 5920, polycaprolactam, PA 66, polyureas, urethane, polycarbodiimide, polybenzimidazole, Ju quinoxaline, tricarboxylic acid Mierocrystalline cellulose, rhodia, soluble cotton, chitin or above-mentioned macromolecule mixture is characterized in that:
(1) it is made by claim 1 or 2 described methods with existing macromolecular material;
(2) solvent that is mixed with the form height molecular solution is formic acid, acetate or their mixture, and precipitation agent is a water, and the protection polymer is polyvinyl alcohol, polyacrylamide, polyvinylpyrrolidone, polyoxyethylene glycol or their mixture.
4. chlorosulfonated polyethylene, polyacetylene, polyvinyl formal, polyvinyl butyral acetal, polyvinyl chloride, polyvinylidene chloride, polyvinylidene difluoride (PVDF), polyvinyl methyl ketone, poly-sulphur vinyl fluoride, polyacrylonitrile, polymethacrylonitrile, polyacrolein, poly-two acryloyl methane, poly acrylic anhydride, polymethacrylic acid anhydride, polyoxymethylene, poly-propionic aldehyde, polyacrolein, polyphenylene oxide, polyetherketone, polysulfones, chloromethyl polysulphone, polyethersulfone, polyether sulphone, polycarbonate, polysulfonamides, polyimide, polyetherimide, polybenzoxazole Ju quinoxaline, methylcellulose gum, rhodia, the cyanoethyl rhodia, three cellulose caproates, the uniform microsphere and the acicular microparticles of three sad Mierocrystalline celluloses or above-mentioned macromolecule mixture is characterized in that:
(1) they all are to make by claim 1 or 2 described methods with existing macromolecular material;
(2) solvent that is mixed with the form height molecular solution is dimethyl formamide, N,N-DIMETHYLACETAMIDE or their mixture, and precipitation agent is a water, and the protection polymer is polyvinyl alcohol, polyacrylamide, polyvinylpyrrolidone, polyoxyethylene glycol or their mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011400226A CN1160398C (en) | 2001-11-21 | 2001-11-21 | High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011400226A CN1160398C (en) | 2001-11-21 | 2001-11-21 | High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1353130A CN1353130A (en) | 2002-06-12 |
| CN1160398C true CN1160398C (en) | 2004-08-04 |
Family
ID=4675595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011400226A Expired - Fee Related CN1160398C (en) | 2001-11-21 | 2001-11-21 | High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1160398C (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006082908A1 (en) * | 2005-02-02 | 2006-08-10 | Ube Industries, Ltd. | Process for producing porous spherical polyamide particle |
| US8574669B2 (en) * | 2008-05-21 | 2013-11-05 | Toray Industries, Inc. | Method for producing polymer fine particle comprising contacting an emulsion with a poor solvent |
| KR20130066618A (en) * | 2010-04-20 | 2013-06-20 | 우베 고산 가부시키가이샤 | Polyamide microparticles, manufacturing method therefor, optical film using said polyamide microparticles, and liquid-crystal display device |
| KR20150051940A (en) * | 2012-08-30 | 2015-05-13 | 도레이 카부시키가이샤 | Method for producing fine vinylidene fluoride resin particles, and fine vinylidene fluoride resin particles |
| CN102964612B (en) * | 2012-08-30 | 2014-10-15 | 北京爱美客生物科技有限公司 | Polyvinyl alcohol-borax microsphere and preparation method thereof |
| CN104262646B (en) * | 2014-09-12 | 2017-07-21 | 中国科学院化学研究所 | The Long Carbon Chain Polyamide powdered base of morphology controllable and the highly conductive composite powder material of morphology controllable |
| CN105001635A (en) * | 2015-07-21 | 2015-10-28 | 上海交通大学 | Ionic liquid and method for preparing aromatic polymer microspheres by adopting ionic liquid as solvent |
| CN105111467B (en) * | 2015-08-27 | 2018-02-23 | 北京化工大学 | A kind of preparation method of the PEI ultrafine powder of size tunable |
| CN106674553B (en) * | 2015-11-11 | 2020-02-11 | 中国科学院理化技术研究所 | Polyamide porous microsphere and preparation method thereof |
| CN107381532A (en) * | 2016-05-17 | 2017-11-24 | 中国科学院大连化学物理研究所 | A kind of synthetic method of polyvinyl chloride-based charcoal bead |
| CN108743929B (en) * | 2018-06-14 | 2021-07-27 | 四川大学 | Preparation method and application of urease gel microspheres used as urea scavenger |
| CN109988322A (en) * | 2019-02-21 | 2019-07-09 | 中国乐凯集团有限公司 | Water-based fluoropolymer emulsion, preparation method and applications |
| CN111995775A (en) * | 2020-09-01 | 2020-11-27 | 安徽美邦树脂科技有限公司 | PVB (polyvinyl butyral) nano particle and preparation method thereof |
| CN114276667B (en) * | 2021-12-30 | 2023-04-18 | 吉林大学 | Crystalline polyaryletherketone microsphere toughened polyaryletherketone material and preparation method thereof |
-
2001
- 2001-11-21 CN CNB011400226A patent/CN1160398C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN1353130A (en) | 2002-06-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1160398C (en) | High-molecular microspheres or acicular microparticles with uniform granularity and its shaping process | |
| CA1329800C (en) | Composite separating agent | |
| DE60012311T2 (en) | NEGATIVELY LOADED MEMBRANES | |
| Lan et al. | Electrospun nanofibrous cellulose diacetate nitrate membrane for protein separation | |
| CN106661263B (en) | Method for producing porous cellulose medium | |
| DE112004001096T5 (en) | polyelectrolyte | |
| SE446453B (en) | CYCLODEXRIN / POLYVINYL ALCOHOL SEGMENT COPOLYMES AND SETS FOR PREPARING THEREOF | |
| JPWO2008084854A1 (en) | Cellulose microparticles and dispersions and dispersions thereof | |
| CN102911379A (en) | Method for preparing cellulose acetate microspheres and product prepared by method | |
| CN101612540A (en) | A kind of is the method that solvent prepares cellulose microsphere with the ionic liquid | |
| CN110227419B (en) | Humic acid/beta-cyclodextrin polymer, composite microsphere and preparation method thereof | |
| DE69834558T2 (en) | Release agents for optical isomers and methods for their preparation | |
| CN114245757A (en) | Ion exchange type nanofiber framework three-dimensional separation material with controllable structure and preparation method thereof | |
| EP3896092A1 (en) | Method for producing cellulose beads | |
| EP0582811A1 (en) | Formed sulfonate groups containing polysiloxanes, process for their preparation and their application | |
| CN106565908B (en) | A kind of preparation method of monodispersed large grain-size polymer microballoon | |
| EP0722362B1 (en) | Process and substrates for gel permeation chromatography | |
| CN101362068B (en) | Precipitation polymerization preparation method of crosslinked polystyrene microspheres | |
| CN109225328B (en) | Chitosan embedded palladium nanofiber catalyst and preparation method and application thereof | |
| CN111217372B (en) | Chiral mesoporous core-shell structure silica nanoparticle and preparation method and application thereof | |
| EP0211223B1 (en) | Spherical grains of poly(alpha-amino acid)and production method thereof | |
| JP2506682B2 (en) | Manufacturing method of spherical particles | |
| JPH082992B2 (en) | Manufacturing method of porous spherical particles | |
| JPH0730202B2 (en) | Manufacturing method of spherical particles | |
| CN100591812C (en) | Preparation method of glycosylated nano-fibre for identifying protein and applications |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |