CN1103408A - Synthesis of random styrene-maleic anhydride copolymer - Google Patents
Synthesis of random styrene-maleic anhydride copolymer Download PDFInfo
- Publication number
- CN1103408A CN1103408A CN 93114923 CN93114923A CN1103408A CN 1103408 A CN1103408 A CN 1103408A CN 93114923 CN93114923 CN 93114923 CN 93114923 A CN93114923 A CN 93114923A CN 1103408 A CN1103408 A CN 1103408A
- Authority
- CN
- China
- Prior art keywords
- maleic anhydride
- weight
- styrene
- polymerization
- reactor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
- C08F212/02—Monomers containing only one unsaturated aliphatic radical
- C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
- C08F212/06—Hydrocarbons
- C08F212/08—Styrene
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
The process for synthesizing random copolymer of styrene-maleic anhydride includes charging part of styrene into reactor, dissolving maleic anhydride in residual styrene, and polymerization by adding dropwise the solution into reactor at 100-130 deg.C and ordinary pressure. Its primary conversion is over 60%. The copolymer is a thermo-plastic material used as modifier and compatilizer with vitrifying temp. of 90-130 deg.C and tension strength of over 30 MPa.
Description
The present invention is a kind of method with substance law synthesizing styrene-maleic anhydride random copolymer.
In macromolecular material, mol ratio is formed the styrene-maleic anhydride copolymer near 1: 1, because it absorbs water easily and is difficult to forming process and can not be used as thermoplastic material.Atactic styrene-maleic anhydride copolymer because wherein maleic anhydride content is lower, makes it have good processing properties.In the free-radical polymerized process of phenylethylene-maleic anhydride, because two kinds of monomeric reactivity ratios differ greatly, make that the tendency that forms alternating structure is stronger, increased the difficulty that obtains low maleic anhydride content random copolymers.In EP-27274, introduced the bulk polymerisation process of vinyl aromatic monomer random copolymers, its process will be at first will charge into first reactor by the vinylbenzene and the maleic anhydride mix monomer of copolymerization theoretical calculate, the postheating reactor is to the temperature of reaction of setting (80～160 ℃), add a certain amount of maleic anhydride then in per 40 minutes or shorter interval, the styrene conversion rate reaches the preset value among 30～60% in system.After rate to be transformed reaches and stablizes, the mix monomer that adds certain metering proportion rapidly, copolymer solution with equivalent causes and second reactor of first reactors in series and the 3rd reactor subsequently simultaneously, and adds in a certain amount of maleic anhydride monomer to the second and the 3rd reactor.This shows, this complex process, complex operation, control is difficult, is difficult to obtain the random copolymers of phenylethylene-maleic anhydride.Because maleic anhydride at room temperature is a solid, very easily moisture absorption adds fashionable also being difficult to quantitatively, so add after needing to introduce the appropriate solvent wiring solution-forming, can bring solvent into like this in polymerization process, makes reaction depart from the direction of pure mass polymerization in addition.For overcoming shortcoming and the problem that exists in the above-mentioned polymerization process, obtain to have the multipolymer of excellent machinability, we have invented a kind of new synthetic method of atactic styrene-maleic anhydride copolymer that obtains.
Polymerization process of the present invention is at first dropping into vinylbenzene in advance in reactor, input amount is 10%～80%(weight of styrene polymerization consumption), be preferably 30%～50%(weight), a certain amount of polymerization is dissolved in wiring solution-forming in the residual styrene polymerization consumption with maleic anhydride, this drips of solution being added to temperature then is 100～130 ℃, be preferably 105～115 ℃, pressure is to go to carry out polyreaction in the non-pressurized reactor.Because this reaction is thermopositive reaction, so rate of addition should make temperature of reaction kettle and still remove hot kept stable outward.Behind the question response 5～10 hours, add the reaction terminating agent Resorcinol of 2～10 ‰ total monomer amounts, then polymers soln is introduced and carried out the vacuum devolatilization in the exhaust screw extrusion press and promptly remove residual monomer.Temperature of charge during the vacuum devolatilization is 100～280 ℃, vacuum tightness is 0.02～0.09MPa, after finishing, devolatilization draws cooling, obtain even, transparent, slick atactic styrene-maleic anhydride copolymer, wherein maleic anhydride content is 5～20%(weight after testing), styrene content is 80～95%(weight), weight-average molecular weight is 2.0 * 10
5～4.0 * 10
5, second-order transition temperature Tg is 90～130 ℃, tensile strength is greater than 30MPa.This method except that the copolyreaction transformation efficiency greater than 60%, polyreaction is milder, control has overcome complex process in the past easily, complex operation, the shortcoming of control difficulty.
The limiting viscosity of atactic styrene-maleic anhydride copolymer also be one than important physical parameter, because polymer substance limiting viscosity [η] and its molecular-weight average have [η]=KM
aRelation.K, a are constant in the formula, and M is a molecular-weight average.
The measuring method of this limiting viscosity is: a certain amount of copolymer product is dissolved in acetone earlier; Filtering the back steams except that acetone; And vacuum-drying made sample in 3 hours, taking by weighing 0.2 gram sample is dissolved in 25 milliliters of butanone, under 30 ℃, butanone solution viscosity number with the determination of ubbelohde viscometer preparation, be the limiting viscosity of polymerization product, the limiting viscosity scope of the inventive method synthetic atactic styrene-maleic anhydride copolymer is 40～50 a milliliters/gram.
Embodiment 1:
708 gram maleic anhydrides are dissolved in wiring solution-forming in the 620 gram vinylbenzene, are added drop-wise in the pre-reactor of throwing the cinnamic band anchor stirrers of 3100 grams, under 110 ℃ of polymerization temperatures, condition of normal pressure, carry out polyreaction.After reaction is carried out 8 hours, add 13 gram Resorcinol, polymers soln to be introduced carried out the vacuum devolatilization in the exhaust screw extrusion press then, this moment, material was 100～280 ℃ in temperature, vacuum tightness is under 0.02～0.09MPa condition, draws cooling then.Even, transparent, the slick atactic styrene-maleic anhydride copolymer that obtains, wherein maleic anhydride content is a 11.0%(weight after testing), styrene content is a 89.0%(weight); Weight-average molecular weight 2.4 * 10
5; Second-order transition temperature Tg is 110 ℃, and tensile strength is 32.4MPa; Limiting viscosity is 47.5 a milliliters/gram, and the styrene conversion rate is 62.0%.
Embodiment 2:
100 gram maleic anhydrides are dissolved in wiring solution-forming in the 600 gram vinylbenzene, are added drop-wise in the reactor of the cinnamic band anchor stirrer of pre-input 300 grams, under 105 ℃ of polymerization temperatures, condition of normal pressure, carry out polyreaction.After reaction is carried out 9.5 hours, add 3.5 gram Resorcinol, polymers soln to be introduced carried out the vacuum devolatilization in the exhaust screw extrusion press then, this moment, material was 100～280 ℃ in temperature, vacuum tightness is under 0.02～0.09MPa condition, draws cooling then.Even, transparent, the slick atactic styrene-maleic anhydride copolymer that obtains, wherein maleic anhydride content is a 11.5%(weight after testing), styrene content is a 88.5%(weight); Weight-average molecular weight 3.0 * 10
5; Second-order transition temperature Tg is 120 ℃, and tensile strength is 38.1MPa; Limiting viscosity is 48.5 a milliliters/gram, and the styrene conversion rate is 66.8%.
Embodiment 3:
90 gram maleic anhydrides are dissolved in wiring solution-forming in the 600 gram vinylbenzene, are added drop-wise in the reactor of the cinnamic band anchor stirrer of pre-input 400 grams,, carry out polyreaction under the condition of normal pressure 120 ℃ of polymerization temperatures.After reaction is carried out 7 hours, add 5.5 gram Resorcinol, polymers soln to be introduced carried out the vacuum devolatilization in the exhaust screw extrusion press then, this moment, material was 100～280 ℃ in temperature, vacuum tightness is under 0.02～0.09MPa condition, draws cooling then.Even, transparent, the slick atactic styrene-maleic anhydride copolymer that obtains, wherein maleic anhydride content is a 13.0%(weight after testing), styrene content is a 87.0%(weight); Weight-average molecular weight 2.1 * 10
5; Second-order transition temperature Tg is 117 ℃, and tensile strength is for being 30.2MPa; Limiting viscosity is 41.7 a milliliters/gram, and the styrene conversion rate is 70.0%.
Embodiment 4:
200 gram maleic anhydrides are dissolved in wiring solution-forming in the 1440 gram vinylbenzene, are added drop-wise in the reactor of the cinnamic band anchor stirrer of pre-input 160 grams, under polymerization temperature is 90 ℃, condition of normal pressure, carry out polyreaction.After reaction is carried out 4.5 hours, add 10 gram Resorcinol, polymers soln to be introduced carried out the vacuum devolatilization in the exhaust screw extrusion press then, this moment, temperature of charge was 100～280 ℃, vacuum tightness is under 0.02～0.09MPa condition, draws cooling then.Even, transparent, the slick atactic styrene-maleic anhydride copolymer that obtains, wherein maleic anhydride content is a 18.5%(weight after testing), styrene content is a 81.5%(weight); Weight-average molecular weight 3.8 * 10
5; Second-order transition temperature Tg is 135 ℃, and tensile strength is 40.5MPa; Limiting viscosity is 45.0 a milliliters/gram, and the styrene conversion rate is 60.5%.
Embodiment 5:
100 gram maleic anhydrides are dissolved in wiring solution-forming in the 400 gram vinylbenzene, are added drop-wise in the reactor of the cinnamic band anchor stirrer of pre-input 1600 grams, under polymerization temperature is 140 ℃, condition of normal pressure, carry out polyreaction.After reaction is carried out 6.5 hours, add 10 gram Resorcinol, polymers soln to be introduced carried out the vacuum devolatilization in the exhaust screw extrusion press then, this moment, material was 100～280 ℃ in temperature, vacuum tightness is under 0.02～0.09MPa condition, draws cooling then.Even, transparent, the slick atactic styrene-maleic anhydride copolymer that obtains, wherein maleic anhydride content is a 6.5%(weight after testing), styrene content is a 93.5%(weight); Weight-average molecular weight is 2.0 * 10
5; Second-order transition temperature Tg is 90 ℃, and tensile strength is 30.1MPa; Limiting viscosity is 46.3 a milliliters/gram, and the styrene conversion rate is 70.5%.
Claims (3)
1, a kind of vinylbenzene 80～95% (weight) that contains, the polymerization process of the atactic styrene-maleic anhydride copolymer of maleic anhydride 5～20% (weight), it is characterized in that maleic anhydride with the polymerization consumption is dissolved in 20%～90% (weight) polymerization with wiring solution-forming in the vinylbenzene amount, be added drop-wise to pre-polymerization vinylbenzene amount of having thrown 10%～80% (weight), temperature is that 100～130 ℃, pressure are to carry out polyreaction in the non-pressurized reactor.
2, polymerization process according to claim 1 is characterized in that dropping in advance that the vinylbenzene amount is the 30%～50%(weight of polymerization with the vinylbenzene amount in the reactor).
3, polymerization process according to claim 1 is characterized in that the temperature in the reactor is 105～115 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93114923A CN1049226C (en) | 1993-12-02 | 1993-12-02 | Synthesis of random styrene-maleic anhydride copolymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93114923A CN1049226C (en) | 1993-12-02 | 1993-12-02 | Synthesis of random styrene-maleic anhydride copolymer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1103408A true CN1103408A (en) | 1995-06-07 |
| CN1049226C CN1049226C (en) | 2000-02-09 |
Family
ID=4990702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN93114923A Expired - Lifetime CN1049226C (en) | 1993-12-02 | 1993-12-02 | Synthesis of random styrene-maleic anhydride copolymer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1049226C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1112384C (en) * | 1998-09-16 | 2003-06-25 | 中国石油化工集团公司 | Styrene-maleic anhydride polymerizing technology |
| CN1300196C (en) * | 2005-07-14 | 2007-02-14 | 浙江大学 | Preparation method of ultra high molecular weight phenylethylene/maleic anhydride copolymer |
| CN102391425A (en) * | 2011-08-31 | 2012-03-28 | 五行材料科技（江苏）有限公司 | Novel compatilizer and preparation method thereof, polyphenylene oxide / polyamide blend alloy containing compatilizer and preparation method thereof |
| CN102993350A (en) * | 2012-09-28 | 2013-03-27 | 天津金发新材料有限公司 | Styrene/maleic anhydride compound and preparation method thereof |
| CN111234081A (en) * | 2020-03-06 | 2020-06-05 | 长春工业大学 | Low-molecular-weight narrow-distribution styrene-maleic anhydride copolymer and preparation method thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5655410A (en) * | 1979-10-15 | 1981-05-16 | Daicel Chem Ind Ltd | Continuous bulk polymerization of styrene type copolymer |
| JPS60147413A (en) * | 1984-01-10 | 1985-08-03 | Idemitsu Petrochem Co Ltd | Production of styrene based resin |
-
1993
- 1993-12-02 CN CN93114923A patent/CN1049226C/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1112384C (en) * | 1998-09-16 | 2003-06-25 | 中国石油化工集团公司 | Styrene-maleic anhydride polymerizing technology |
| CN1300196C (en) * | 2005-07-14 | 2007-02-14 | 浙江大学 | Preparation method of ultra high molecular weight phenylethylene/maleic anhydride copolymer |
| CN102391425A (en) * | 2011-08-31 | 2012-03-28 | 五行材料科技（江苏）有限公司 | Novel compatilizer and preparation method thereof, polyphenylene oxide / polyamide blend alloy containing compatilizer and preparation method thereof |
| CN102993350A (en) * | 2012-09-28 | 2013-03-27 | 天津金发新材料有限公司 | Styrene/maleic anhydride compound and preparation method thereof |
| CN102993350B (en) * | 2012-09-28 | 2014-12-24 | 天津金发新材料有限公司 | Styrene/maleic anhydride compound and preparation method thereof |
| CN111234081A (en) * | 2020-03-06 | 2020-06-05 | 长春工业大学 | Low-molecular-weight narrow-distribution styrene-maleic anhydride copolymer and preparation method thereof |
| CN111234081B (en) * | 2020-03-06 | 2022-12-20 | 长春工业大学 | Low-molecular-weight narrow-distribution styrene-maleic anhydride copolymer and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1049226C (en) | 2000-02-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3972961A (en) | Process for the preparation of graft copolymers | |
| USRE30754E (en) | Process for the preparation of graft copolymers | |
| CN1049226C (en) | Synthesis of random styrene-maleic anhydride copolymer | |
| Lu et al. | Microwave radiation solid‐state copolymerization in binary maleic anhydride—dibenzyl maleate systems | |
| Iwatsuki et al. | Equilibrium polymerizations of 7, 8-dibenzoyl-, 7, 8-diacetyl-, and 7, 8-dibutoxycarbonyl-7, 8-dicyanoquinodimethane and their copolymerizations with styrene: a new concept on the mechanism of alternating copolymerization | |
| Hamurcu et al. | Polystyrene-b-polydimethyl siloxane (PDMS) multicomponent polymer networks: styrene polymerization with macromonomeric initiators (macroinimers) having PDMS units | |
| Chiang et al. | Studies of reactions with polymers. III. Syntheses and properties of poly (vinyl alcohol) graft terpolymers | |
| Wang et al. | Polyurethane–acrylate hybrid latexes from miniemulsion polymerization: effect of endgroups on structure and properties | |
| US3337648A (en) | Graft copolymer comprising the reaction product of a carboxy-terminated conjugated diene polymer with a vinyl aromatic hydrocarbon and a lactam | |
| Zhang et al. | Preparation of functional polymers by living anionic polymerization: Polymerization of allyl methacrylate | |
| Markley et al. | Grafting reactions of vinyl acetate onto poly [(vinyl alcohol)‐co‐(vinyl acetate)] | |
| CN1117786C (en) | Process for preparing modified aliphatic superbranched polyester used to synthesize high-absorbency resin | |
| CN1112384C (en) | Styrene-maleic anhydride polymerizing technology | |
| Kim et al. | Bulk polymerization of ε-caprolactone in an internal mixer and in a twin screw extruder | |
| Song et al. | Grafting of 2‐(dimethylamino) ethyl methacrylate on linear low density polyethylene in the melt | |
| Angelovici et al. | Copolymerization of acrylic esters with ethyl α‐cyanocinnamate | |
| Otsu et al. | Monomer‐isomerization radical polymerization of di‐tert‐butyl maleate and preparation of poly (fumaric acid) via pyrolysis | |
| Jia et al. | Copolymerization of ethyl α‐(hydroxymethyl) acrylate with maleimide and characterization of the resulting copolymer | |
| JPH0460127B2 (en) | ||
| Jiang et al. | Kinetics for copolymerization of methyl methacrylate with N‐cyclohexylmaleimide | |
| Liebersohn et al. | Polymers with pendant isocyanate groups. I. Dual synthesis and properties of poly (styrene‐co‐styryl isocyanate) | |
| CN1035476C (en) | Synthesis for copolymer of alternant phenylethylene & butadiene diacid anhydride | |
| CN1218973C (en) | Synthetic method of acrylic acid series copoly-macromolecule damping material | |
| Ueda et al. | Radical‐initiated homo‐and copolymerization of methoxymethyl methacrylate | |
| CN115160512B (en) | Lignin-based thermoplastic elastomer with rapid repair function and preparation method thereof |
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 | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20131202 Granted publication date: 20000209 |
|
| DD01 | Delivery of document by public notice |
Addressee: China Petrochemical Corporation Document name: Notification of Expiration of Patent Right Duration |