CN1727395A - Fusible polyacrylonitrile resin in low melting point - Google Patents
Fusible polyacrylonitrile resin in low melting point Download PDFInfo
- Publication number
- CN1727395A CN1727395A CN 200410053229 CN200410053229A CN1727395A CN 1727395 A CN1727395 A CN 1727395A CN 200410053229 CN200410053229 CN 200410053229 CN 200410053229 A CN200410053229 A CN 200410053229A CN 1727395 A CN1727395 A CN 1727395A
- Authority
- CN
- China
- Prior art keywords
- polyacrylonitrile resin
- additive
- resin
- melting point
- low melting
- 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
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
A fusible polyacrylonitrile resin with low fusion point (lower than 200 deg.C) is proportionally prepared from a solid additive and a fusible polyacrylonitrile resin through mechanical mixing. Said additive is chosen from sweet alcohol, hydroquinone and their mixture. Said fusible polyacrylonitrile resin is the copolymer of acrylonitrile and the second unit chosen from perspex, methylacrylonitrile and butenenitrile.
Description
Technical field
The present invention relates to a kind of fusible polyacrylonitrile resin, particularly a kind of by adding the low melting point fusible polyacrylonitrile resin that solid additive obtained.
Background technology
Polyacrylonitrile resin is the wider superpolymer of a kind of purposes, particularly adopts the fibre property of acrylic resin manufacturing to exactly like wool, occupies very big proportion in the synthon production.But a defective of polyacrylonitrile resin is a fusing point (theoretical value is 319 ℃) is higher than decomposition temperature (being generally 250 ℃), therefore it can't be processed with the fused method, polyacrylonitrile fibre also can only be used the method manufacturing of solvent spinning usually, this spinning processes will use a large amount of poisonous and harmfuls or mordant solvent, must carry out the recovery and the purification of solvent in process of production, and must wash and drying etc. fiber, so complex process and environmental pollution are serious.
For many years, reduce the research of polyacrylonitrile fusing point and quite paid close attention to, and obtained gratifying progress.In prior art, more in the past is to adopt the water plasticising method of (comprising low molecular solvent plasticising), water or other low molecular solvent can make this mixture be molten state under lower temperature after polyacrylonitrile resin is soaked into, but when adopting this kind method to carry out melt-spinning, easily produce cavity filament, fracture of wire, lousiness, fiber also can exist internal capillary and surface imperfection, thereby causes fibre property to descend greatly, so also there is more problem in suitability for industrialized production.
Become the focus of exploitation fusible polyacrylonitrile resin in recent years as internally plasticized chemical modification method, it is to introduce the comonomer that can form flexible chain on the polyacrylonitrile macromolecular chain, thereby reduce the fusing point of polyacrylonitrile, make fusible polyacrylonitrile resin.This comonomer mainly comprises methyl methacrylate and methacrylonitrile, and the crotononitrile that proposed of Chinese patent application 02136955.0.The fusible polyacrylonitrile resin that obtains by chemical modification method should belong to fusible polyacrylonitrile resin truly.But, existing fusible polyacrylonitrile resin fusing point is generally all between 200 ℃ to 250 ℃, yet studies show that, be subjected to the different molecule regularities and the influence of different molecular weight, when temperature during near 200 ℃ the polyacrylonitrile molecule existed part to decompose, so the optimal processing fusing point of fusible polyacrylonitrile resin is to be lower than 200 ℃.Although can further reduce the fusing point of fusible polyacrylonitrile resin by the content that increases comonomer, but too high content can have influence on the original proterties of polyacrylonitrile, will change the original style of polyacrylonitrile fibre with the fiber of this polyacrylonitrile resin manufacturing.
Summary of the invention
The invention provides a kind of low-melting fusible polyacrylonitrile resin, the technical problem that it will solve is that this fusible polyacrylonitrile resin of requirement possesses the processing fusing point that is lower than 200 ℃, and the resin behind the processing characteristics of resin itself and the reduction fusing point then can not produce detrimentally affect to the product performance that make.
Below be the technical scheme that the present invention solves the problems of the technologies described above:
A kind of low melting point fusible polyacrylonitrile resin, this resin is the uniform mixture that a kind of solid-state additive and fusible polyacrylonitrile resin obtain by mechanically mixing, additive is taken from a kind of in sweet and pure or the Resorcinol, or be both mixture, the weight ratio of additive and polyacrylonitrile resin is 1: (10～50), additive are that granularity is less than 200 purpose powder or fine particles.Fusible polyacrylonitrile resin is the multipolymer that the vinyl cyanide and the second copolymerization units copolymerization form, second copolymerization units is methyl methacrylate, methacrylonitrile or crotononitrile, is that the content of benchmark second copolymerization units in multipolymer is 10～18wt% with the total amount of all polymerized units.
Above-mentioned additive is preferably sweet and pure; Additive and polyacrylonitrile resin blended weight ratio are preferably additive: polyacrylonitrile resin=1: (12～30).
The viscosity-average molecular weight of polyacrylonitrile resin generally can be 20000～60000 in the technique scheme.
Polyacrylonitrile resin then no longer needs other to improve the second flexible monomer the multipolymer as being used for making polyacrylonitrile fibre, but in order to obtain good dyeing behavior, the 3rd monomer that is used for dyeing, modifying will need.Therefore, also can contain the 3rd copolymerization units methylpropene sodium sulfonate in the above-mentioned polyacrylonitrile resin, methylpropene sodium sulfonate is that the content of benchmark is 0.2～1.0wt% with the total amount of all polymerized units.
Analyze from principle, technical scheme provided by the invention also do not require and limits the concrete kind of second copolymerization units that makes polyacrylonitrile reduce fusing point, more than these second copolymerization units only be that the contriver recommends.The known in fact this copolymerization units with same function has also comprised the monomeric multipolymer of other unsaturated olefin, as being vinylformic acid, esters of acrylic acid and derivative thereof; Toxilic acid (maleic anhydride), maleic acid ester class and derivative thereof; Propene sulfonic acid, propene sulfonic acid salt and derivative thereof; Haloalkene hydro carbons, acrylamide and derivative thereof; Styrenic and vinyl esters organism or the like.Those skilled in the art can know the technical program by inference and be applied to also will obtain identical effect by the fusible polyacrylonitrile resin that other similar copolymerization units and acrylonitrile compolymer obtain.
We know why polyacrylonitrile resin has high melt point is that therefore the interaction force of weakening-CN group just can reduce the fusing point of polyacrylonitrile resin because contain strong polar group-CN in its molecular chain.The additive that contains in the fusible polyacrylonitrile resin provided by the invention is a kind of compound that contains hydrogen bond, the contriver found through experiments this compound and can weaken greatly-interaction force of CN group, and weaken cyclic action between adjacent-CN group, thereby can reduce the fusing point of polyacrylonitrile significantly.And because this additive is that granularity is less than 200 purpose powder or fine particles, it will be evenly distributed in the melt after the polyacrylonitrile resin fusion, unlike adopting water or low molecular solvent plasticising to reduce the method for polyacrylonitrile resin fusing point, because of the evaporation of water or solvent will cause having bubble in the melt, thereby finally influence the mechanical property of resin such as fiber.
The fusing point of fusible polyacrylonitrile resin is downward trend with the increase of additive level, and the contriver found through experiments the weight ratio of additive and polyacrylonitrile resin 1: be proper in the scope of (10～50).The additive reduction of fusing point after a little while is not obvious, with the physicals of impact polypropylene nitrile resin, all can produce in various degree influence to spinning property and quality of fiber especially when resin is used to make fiber when additive is too much.
Compared with prior art, positive effect of the present invention is that its processing fusing point of fusible polyacrylonitrile resin that provides is reduced to below 200 ℃, has thoroughly avoided fusible polyacrylonitrile issuable decomposition in the melt-processed process.Because the melting index of resin obviously improves, the flowing property of melt also improves simultaneously, and this is highly beneficial to the processing characteristics that improves resin.
Below will the invention will be further described by specific embodiment.
Embodiment
Fusing point adopts the sensible heat analysis-e/or determining among the embodiment, temperature rise rate: 3 ℃/minute is fusing point with the temperature during the whole fusion of polymkeric substance on the instrument; Melting index adopts the melt flow rate (MFR) instrument to measure, mouthful mould: diameter 2.095mm, length 8mm; Viscosity-average molecular weight adopts Ubbelohde viscometer to measure specific viscosity η
Sp, obtain by conversion then.
[embodiment 1]
Get fusible polyacrylonitrile resin and additive and join in the open container that whipping appts 2L is housed by required weight ratio, stir about 15min, even until additive and mixed with resin.Additive is crushed to Powdered additive or fine particulate earlier as there being bulk, requires granularity to be no more than 200 orders.
Fusible polyacrylonitrile resin is the multipolymer of vinyl cyanide and methyl methacrylate, total amount with all polymerized units is that the content of benchmark methyl methacrylate in multipolymer is 15wt%, the viscosity-average molecular weight of resin is 4000, the fusing point of resin is 240 ℃, and 240 ℃ of melting index that record are the 11g/10 branch.
[embodiment 2～8]
Fusible polyacrylonitrile resin is the multipolymer of vinyl cyanide and crotononitrile, is that the content of benchmark crotononitrile in multipolymer is 14wt% with the total amount of all polymerized units, and the viscosity-average molecular weight of polyacrylonitrile resin is 3500.All the other are with embodiment 1
It is 1 listed that concrete additive, additive and the polyacrylonitrile resin blended weight ratio that adopts of each embodiment, the fusing point of mixture and melting index see Table.
Further the low melting point fusible polyacrylonitrile resin that obtains with embodiment 2～8 is a raw material, adopts the technology of melt-spinning to carry out spinning, makes the acrylic fiber of 1.46dtex, the breaking tenacity and the extension at break of test fiber, and it the results are shown in Table 2.
Table 1.
| Additive | Additive/resin (weight ratio) | Fusing point (℃) | Melting index (g/10min) | |
| Embodiment 1 | Sweet and pure | 1/16 | 182 | 27.2 |
| Embodiment 2 | Sweet and pure | 1/10 | 166 | 36.0 |
| Embodiment 3 | Sweet and pure | 1/12 | 173 | 30.9 |
| Embodiment 4 | Sweet and pure | 1/30 | 190 | 22.6 |
| Embodiment 5 | Sweet and pure | 1/49 | 195 | 16.4 |
| Embodiment 6 | Resorcinol | 1/12 | 175 | 30.3 |
| Embodiment 7 | Resorcinol | 1/15 | 187 | 26.2 |
| Embodiment 8 | Resorcinol | 1/20 | 192 | 18.6 |
Table 2.
| Breaking tenacity (CN/dtex) | Extension at break (%) | |
| Embodiment 2 | 2.8 | 30 |
| Embodiment 3 | 3.0 | 28 |
| Embodiment 4 | 3.6 | 21 |
| Embodiment 5 | 3.8 | 20 |
| Embodiment 6 | 2.8 | 29 |
| Embodiment 7 | 3.1 | 26 |
| Embodiment 8 | 3.4 | 23 |
Claims (5)
1, a kind of low melting point fusible polyacrylonitrile resin, this resin is the uniform mixture that a kind of solid-state additive and fusible polyacrylonitrile resin obtain by mechanically mixing, additive is taken from a kind of in sweet and pure or the Resorcinol, or be both mixture, the weight ratio of additive and polyacrylonitrile resin is 1: (10～50), additive is that granularity is less than 200 purpose powder or fine particles, fusible polyacrylonitrile resin is the multipolymer that the vinyl cyanide and the second copolymerization units copolymerization form, second copolymerization units is a methyl methacrylate, methacrylonitrile or crotononitrile are that the content of benchmark second copolymerization units in multipolymer is 10～18wt% with the total amount of all polymerized units.
2, low melting point fusible polyacrylonitrile resin according to claim 1 is characterized in that at described additive being sweet and pure.
3, low melting point fusible polyacrylonitrile resin according to claim 1 is characterized in that the weight ratio at described additive and polyacrylonitrile resin is 1: (12～30).
4, according to claim 1,2 or 3 described low melting point fusible polyacrylonitrile resins, the viscosity-average molecular weight that it is characterized in that described polyacrylonitrile resin is 20000～60000.
5, according to claim 1,2 or 3 described low melting point fusible polyacrylonitrile resins, it is characterized in that containing in described polyacrylonitrile resin the 3rd copolymerization units methylpropene sodium sulfonate, is that the content of methylpropene sodium sulfonate in the benchmark multipolymer is 0.2～1.0wt% with the total amount of all polymerized units.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100532298A CN100348659C (en) | 2004-07-29 | 2004-07-29 | Fusible polyacrylonitrile resin in low melting point |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100532298A CN100348659C (en) | 2004-07-29 | 2004-07-29 | Fusible polyacrylonitrile resin in low melting point |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1727395A true CN1727395A (en) | 2006-02-01 |
| CN100348659C CN100348659C (en) | 2007-11-14 |
Family
ID=35926930
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100532298A Expired - Fee Related CN100348659C (en) | 2004-07-29 | 2004-07-29 | Fusible polyacrylonitrile resin in low melting point |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100348659C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109401163A (en) * | 2018-10-11 | 2019-03-01 | 天津工业大学 | A kind of fusible polyacrylonitrile-radical resin, preparation method and applications |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2125242A1 (en) * | 1993-06-17 | 1994-12-18 | Benedict S. Curatolo | Nonwoven fabrics from high nitrile copolymers |
| CA2134823A1 (en) * | 1993-11-10 | 1995-05-11 | Richard C. Smierciak | Process for making a polymer of acrylonitrile, methacrylonitrile and olefinically unsaturated monomers |
| WO2000050509A1 (en) * | 1999-02-22 | 2000-08-31 | The Standard Oil Company | Lubricants for melt processable multipolymers of acrylonitrile and olefinically unsaturated monomers |
| CN1465648A (en) * | 2002-06-17 | 2004-01-07 | 中国人民解放军第二军医大学 | Phase change energy storage composite material and preparation process thereof |
| CN1189491C (en) * | 2002-09-12 | 2005-02-16 | 中国石化上海石油化工股份有限公司 | Fusible polyacrylonitrile resin |
-
2004
- 2004-07-29 CN CNB2004100532298A patent/CN100348659C/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109401163A (en) * | 2018-10-11 | 2019-03-01 | 天津工业大学 | A kind of fusible polyacrylonitrile-radical resin, preparation method and applications |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100348659C (en) | 2007-11-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE69532763T2 (en) | THERMOPLASTIC RESIN COMPOSITION, INJECTION MOLDING AND INJECTION MOLDING BODY | |
| EP0150931B1 (en) | Reinforced composite structures | |
| CN100349937C (en) | Cellulosine plastic composite compatiblizing agent and method for making same | |
| CN101698965B (en) | Absorbing fiber and manufacturing method thereof | |
| CN102504471A (en) | ABS (acrylonitrile-butadiene-styrene)/fiberglass composite material and preparation method thereof | |
| CN104630923A (en) | Method for preparing carbon nano tube modified polyacrylonitrile fibers with solution in-situ polymerization technology | |
| CN101074287A (en) | Production of cellulose/polyacrylonitrile homogeneous mixed solution | |
| CA2400709C (en) | Process for producing highly homogeneous cellulose solution | |
| CN1912003A (en) | Heat resistant nylon material containing thormotropic liquid crystal polymer and its preparation method | |
| CN101435119A (en) | Preparation of modified polyacrylonitrile fibre | |
| CN104987596A (en) | Method for improving surface tension of polypropylene and application for obtained product | |
| DE69824127T2 (en) | Compound high nitrile filaments | |
| CN1727395A (en) | Fusible polyacrylonitrile resin in low melting point | |
| CN100354360C (en) | Method for lowering melting point of fusible polyacrylonitrile resin | |
| CN1727397A (en) | Fusible polyacrylonitrile resin in low melting point | |
| CN100354362C (en) | Method for lowering melting point of fusible polyacrylonitrile resin through additive | |
| CN100354361C (en) | Method for lowering melting point of fusible polyacrylonitrile resin | |
| CN1727396A (en) | Combination of Fusible polyacryonitrile resin in low melting point | |
| CN1189491C (en) | Fusible polyacrylonitrile resin | |
| CN110204874A (en) | A kind of preparation method enhancing vertical structure lactic acid composite material using Lyocell fiber fibrillation | |
| CN1304417A (en) | Polyacrylonitrile particles by surfmer polymerization and sodium removal by chemical exhcnage | |
| CN114316314B (en) | TLCP-para-aramid pulp composite material and preparation method thereof | |
| CN116199975B (en) | Polypropylene modified material and preparation method and application thereof | |
| CN114181488B (en) | Preparation method of composite toughening agent for nylon and product thereof | |
| CN109851947B (en) | High-molecular plasticized PVC3D printing material 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071114 Termination date: 20110729 |