CN1121087A - Synthesis of thermatropic ciquid crystal polyester imide - Google Patents
Synthesis of thermatropic ciquid crystal polyester imide Download PDFInfo
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- CN1121087A CN1121087A CN 94116639 CN94116639A CN1121087A CN 1121087 A CN1121087 A CN 1121087A CN 94116639 CN94116639 CN 94116639 CN 94116639 A CN94116639 A CN 94116639A CN 1121087 A CN1121087 A CN 1121087A
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- monomer
- imide
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- liquid crystal
- antimonous oxide
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Abstract
Under the action of diantimony trioxide and/or zinc acetate, p-hydroxybenzoic acid, binary acid containing imide bond and aromatic dihydric alcohol monomers are directly synthesized into polyester imide as a new-type liquid crystal material. Through the regulation of monomer proportion, liquid crystal polyester imide of different vitrification point and molten temp. is synthesized.
Description
It is imido synthetic to the invention belongs to the thermatropic ciquid crystal macromolecule polyester.
The thermotropic liquid crystalline polymer material has been subject to people's attention day by day as a kind of material with excellent performance since the eighties industrialization in mid-term.Germany Kriche1dorf, the H.R.1987 reported first study on the synthesis of thermotropic liquor polyester imide, thereby developed a kind of thermatropic ciquid crystal polymer.Such liquid crystal polymer not only contains ester bond but also contain imide bond, combine the excellent properties of polyester and polyimide, be expected to become a class heat-resistant engineering plastic, liquid crystal is given its some special performances again, as: excellent thermal characteristics, mechanical property, lower linear expansivity, higher auto-orientation performance etc.
Day disclosure special permission communique 80-91818 is the N of 4-8 with P-hydroxybenzoic acid, Resorcinol, terephthalic acid, carbonatoms, N '-alkylene-α, ω-two-trimellitic acid imide (I) has prepared polyester-imide, because second-order transition temperature is lower, is mainly used in fiber and compressing tablet.
Bab é, it is the N of 2-6 that S.G. adopts carbonatoms, N '-alkylene-α, ω-two-trimellitic acid imide (I) has made thermotropic liquor polyester imide (Makromol.Chem.21 with biphenyl bis-phenol ester, 65-77,1972.), owing to there are many shortcoming face using values little.In patent DE3516427A1, the Kricheldorf of Germany, it is the N of 8-16 that H.R. adopts carbon atom, N '-alkylene-α, ω-two-trimellitic acid imide (I) has made polyester-imide with '-biphenyl diphenol (II) by ester-interchange method, silylanizing method.
Wherein X is a 1-7 carbon atom alkylene, the cycloalkanes support of 5-12 carbon atom, O, S, SO, SO
2, CO, and their center alkyl derivative.
Dike, H.R. by P-hydroxybenzoic acid and contain imide bond alcohol acid (III) and adopt ester-interchange method to synthesize the polyester-imide of high thermal stability, the range of catalysts that he selects for use is wider: Lewis acid, haloid acid, oxide compound, hydride, halogenide, phenates, inorganic salt, organic salt, the double salt of alkaline-earth metal or mixed salt etc.
In patent EP0293713, Kricheldorf, H.R. combine patent DE-OS 2025971 and DE-OS 3516427 adopts direct melt polycondensation method and ester-interchange method to synthesize polyester-imide by P-hydroxybenzoic acid and unit IV, V.
N is the integer of 3-12.HO—Ar—OH????(V)
Wherein monomer V is 1,4-penylene or 4,4 '-biphenylene or their mixture.
The objective of the invention is with P-hydroxybenzoic acid, contain the imide bond diprotic acid and various aromatic dicarboxylic phenol is monomer, at The catalytic antimony trioxide, zinc acetate, manganese acetate, and under the antimonous oxide/zinc acetate, antimonous oxide/manganese acetate effect, adopt direct melt polycondensation/process for solid state polycondensation synthesizing new polyester-imide liquid crystal polymer, by monomer ratio adjustment being synthesized the serial thermotropic liquid crystalline polymer of different glass transformation and melt temperature.
1. the monomer and the structure of the present invention's employing are:
1. P-hydroxybenzoic acid
2. contain soft segment imide bond dicarboxylic acid monomer:
Wherein n is the integer of 4-12;
3. aromatic dicarboxylic phenol: HO-Ar-OH
Wherein Ar refers to:
(1,4-, 2,6-, 2,7-),
Wherein Y is O, S, SO
2, CO, C (CH
3)
2, and alkyl-substituted derivative.
The consumption of P-hydroxybenzoic acid is 20-80mol%, and the monomer ratio of diprotic acid and dihydric phenol (mol) is: 0.98: 1-1.02: 1.
2. the catalyzer that adopts among the present invention has: antimonous oxide, zinc acetate, manganese acetate, 2.5), (2.5: 1-1: 2.5) composite catalyst, input amount account for the 0.01-0.2wt% of monomer otal investment to antimonous oxide/manganese acetate and antimonous oxide/zinc acetate (2.5: 1-1:.
Under above-mentioned catalyst system, monomer and proportioning, be reaction medium with the acetic anhydride, under the nitrogen protection, in 200-250 ℃ of following pre-polymerization 2-4h.Afterwards, be warming up to 290-320 ℃ rapidly, high temperature polymerization 2-4h, the sealed reaction system is kept vacuum tightness between 133-665Pa then, melt continues down polyreaction 2-8h, obtain good toughness, can fine-fibred brown product, yield is 90-98%.
The gained liquid crystal polymer fibre places under 190-250 ℃, keeps vacuum tightness and carry out the solid phase post polymerization between 133-250Pa, can obviously improve the mechanical strength of fiber and the molecular weight of polymkeric substance.
The polyester-imide liquid crystal polymer adopts under 25 ℃ of the Ubbelohde viscometers and records range of viscosities 0.45-0.65 in the mixed solvent of trifluoroacetic acid/dichloromethane (volume ratio 25/2).
By the liquid crystal polymer among the present invention performance resins PES-C, PEK-C, PI, PES, PEEK etc. are carried out modification, wherein liquid crystal material content is 2.0-30wt%, prepared in-situ composite is on the basis of the comprehensive physical and mechanical property that does not reduce matrix resin, can reduce melt viscosity, tonnage and the processing temperature of resin significantly, thereby improve the melt processability of matrix resin.
Polyaryletherketone PEK-C50, PEK-C63 is respectively the performance resins of injection stage and mold pressing level, with the thermotropic liquor polyester imide among the present invention and polyaryletherketone by melt blending (liquid crystal content is 10wt%), can obviously reduce melt viscosity, processing temperature and the tonnage of matrix resin, the comprehensive mechanical property of matrix resin and blend thereof sees Table 1.
The comparison of table 1.LCP/PEK-C blend and matrix resin mechanical property
| Performance PEK-C50/LCP | ???PEK-C63/LCP | ??PEK-C50 | ???PEK-C63 |
| Hot strength (MPa) 108 stretch moduluses (GPa) 2.49 elongation at breaks (%) 9.13 bending strengths (MPa) 172 bending moduluses (GPa) 2.92 impact strength non-notch (KJ/m2) 170.6 breach (J/m), 32.2 glass transitions (℃) | ?????110 ?????3.77 ?????7.28 ?????169 ?????2.71 ?????214.8 ?????32.2 ?????206 | ????105 ????1.76 ????39.9 ????166 ????3.10 ????147 ????70 | ????102 ????2.43 ????6.1 ????132 ????2.74 ????— ????46 ????219 |
Embodiment 1
Mechanical stirrer is being housed; condenser; water separator; have in the there-necked flask of 2L of nitrogen gangway; drop into P-hydroxybenzoic acid 41.5g (0.30mol), 4,4 '-dihydroxy benzophenone 75.0g (0.35mol); imide diacid (n=6) 162.6g (0.35mol); and acetic anhydride 250ml, manganese acetate 0.03g, antimonous oxide 0.04g; reaction flask is placed the aluminium heating jacket; under nitrogen protection, temperature is elevated to and makes system keep reflux state 2h. about 250 ℃, steams then and removes acetic acid; water and excessive acetic anhydride; be warmed up to 300 ℃ rapidly; insulation 2h. removes water separator, closes nitrogen; decompression is evacuated to 665Pa under this temperature; keep 2h., under molten state, take out product, get product 252g; productive rate: 91%; glass transition temperature Tg: 92 ℃, melt temperature Tm:227 ℃, limiting viscosity: 0.23.Fusing sample can be observed birefringent phenomenon under polarizing microscope, have the texture of nematic liquid crystal characteristic.
Embodiment 2
Experimental technique adds P-hydroxybenzoic acid 69.1g (0.5mol), 4 with embodiment 1,4 '-dihydroxy benzophenone 53.6g (0.25mol), contain imide bond diprotic acid (n=6) 116.1g (0.25mol), acetic anhydride 250ml, zinc acetate 0.05g, antimonous oxide 0.06g, get product 210g, productive rate: 95%, glass transition temperature Tg: 89 ℃, melt temperature Tm:215 ℃, limiting viscosity: 0.60.Gained brown product is easy to directly pull into more tough silk, and its mechanical property is inversely proportional to the diameter of the silk that is pulled into, and the silk degree of orientation of just healing thin is higher, and mechanical property better.
The mechanical property of table 2. polyester-imide silk and its diameter concern *
* be result behind solid phase polycondensation in the bracket
| ?????d ????(mm) | ??????stress ???????(MPa) | ????????strain ?????????(％) | ??????modulus ???????(MPa) |
| ????1.58 ????0.70 ????0.65 ????0.50 | ????130.6(153.6) ????144.2(194.3) ????150.7(215.6) ????164.1(260.8) | ????????19.7(15.3) ????????12.4(9.6) ????????7.1?(5.4) ????????6.7?(4.3) | ??????2032(2983) ??????3291(4279) ??????3291(4721) ??????3887(5227) |
Embodiment 3
Experimental technique drops into monomer P-hydroxybenzoic acid 96.7g (0.7mol), imide diprotic acid (n=6) 69.7g (0.15mol) with embodiment 1,4,4 '-dihydroxy benzophenone 32.1g (0.15mol), and acetic anhydride 250ml, zinc acetate 0.07g gets product 172g, productive rate: 96%.Glass transition temperature Tg: 75 ℃ melt temperature Tm:207 ℃, limiting viscosity: 0.45.Sample is observed birefringent phenomenon under polarizing microscope, have the nematic liquid crystal characteristic.
Embodiment 4
Experimental technique drops into monomer P-hydroxybenzoic acid 69.1g (0.5mol) with embodiment 1, contains imide bond diprotic acid (n=6) 116.1g (0.25mol), 1,4-naphthalenediol 40g (0.25mol), and acetic anhydride 250ml, zinc acetate 0.04g, antimonous oxide 0.04g, products therefrom have tangible nematic liquid crystal feature, and very strong toughness is arranged, altogether product 192g, productive rate: 93%, glass transition temperature Tg: 104 ℃, melt temperature Tm:267 ℃, limiting viscosity: 0.29.
Embodiment 5
Experimental technique is with embodiment 1, drop into monomer P-hydroxybenzoic acid 69.1g (0.5mol), imide diprotic acid (n=8) 123.1g (0.25mol), Resorcinol 27.5g (0.25mol), and acetic anhydride 250ml, antimonous oxide 0.08g, products therefrom have tangible nematic liquid crystal feature, altogether product 190g, productive rate: 95%.
Embodiment 6
Experimental technique is with embodiment 1, monomer P-hydroxybenzoic acid 96.7g (0.7mol), imide diprotic acid (n=4) 65.5g (0.15mol), Resorcinol 16.5g (0.15mol), and acetic anhydride 250ml, manganese acetate 0.08g, products therefrom have tangible nematic liquid crystal feature, get product 152g, productive rate: 95%.
Claims (1)
1. imido synthetic method of thermatropic ciquid crystal macromolecule polyester.It is characterized in that adopting direct melt polycondensation/process for solid state polycondensation synthetic, synthesis step is as follows:
1. the monomer and the structure of the present invention's employing are:
A. P-hydroxybenzoic acid:
B. contain soft segment imide bond dicarboxylic acid monomer:
Wherein n is the integer of 4-12;
C. aromatic dicarboxylic phenol: HO-Ar-OH
Wherein Ar refers to:
(1,4-, 2,6-, 2,7-),
Wherein Y is O, S, SO
2, CO, C (CH
3)
2, and alkyl-substituted derivative.
Wherein the consumption of P-hydroxybenzoic acid is 20-80mol%, and the monomer ratio of diprotic acid and dihydric phenol (mol) is 0.98: 1-1.02: 1;
2. the catalyzer that adopts among the present invention has: antimonous oxide, zinc acetate, manganese acetate, 2.5), (2.5: 1-1: 2.5) composite catalyst, input amount account for the 0.01-0.2wt% of monomer otal investment to antimonous oxide/manganese acetate and antimonous oxide/zinc acetate (2.5: 1-1:.
3. under above-mentioned catalyst system, monomer and proportioning, with the acetic anhydride is reaction medium, under the nitrogen protection, in 200-250 ℃ of following pre-polymerization 2-4h, afterwards, be warming up to 290-320 ℃ rapidly, high temperature polymerization 2-4h, sealed reaction system then, keep vacuum tightness between 133-665Pa, melt continues down polyreaction 2-8h, obtain good toughness, can fine-fibred brown product, yield is 90-98%;
4. the gained liquid crystal polymer fibre places under 190-250 ℃, keeps vacuum tightness and carry out solid phase post polymerization 4-8h between 133-250Pa, obtains high mechanical strength and high molecular liquid crystalline polymers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94116639A CN1034339C (en) | 1994-10-20 | 1994-10-20 | Synthesis of thermatropic ciquid crystal polyester imide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94116639A CN1034339C (en) | 1994-10-20 | 1994-10-20 | Synthesis of thermatropic ciquid crystal polyester imide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1121087A true CN1121087A (en) | 1996-04-24 |
| CN1034339C CN1034339C (en) | 1997-03-26 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN94116639A Expired - Fee Related CN1034339C (en) | 1994-10-20 | 1994-10-20 | Synthesis of thermatropic ciquid crystal polyester imide |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323097C (en) * | 2002-06-12 | 2007-06-27 | 三菱化学株式会社 | Process for producing polyester resin |
| CN101560294B (en) * | 2009-05-19 | 2011-11-09 | 中山大学 | Compatible thermotropic liquid crystal polymer and method and application thereof |
| CN101508897B (en) * | 2009-03-11 | 2011-11-09 | 中山大学 | Novel spinnable thermotropic liquor polyester imide, synthesis and uses thereof |
| CN106810695A (en) * | 2017-01-12 | 2017-06-09 | 苏州大学 | A kind of aromatic polyesterimides and preparation method thereof |
| CN109825082A (en) * | 2019-02-10 | 2019-05-31 | 成都其其小数科技有限公司 | A kind of polyesterimide/bismaleimide resin composite material and preparation method |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3516427A1 (en) * | 1985-05-08 | 1986-11-13 | Bayer Ag, 5090 Leverkusen | Thermotropic aromatic polyester-imides having improved heat distortion resistance, process for their preparation, and their use for the production of mouldings, filaments, fibres and films |
| DE3718396A1 (en) * | 1987-06-02 | 1988-12-22 | Bayer Ag | THERMOTROPE POLYESTERIMIDES WITH EXCELLENT PROCESSABILITY, METHOD FOR THE PRODUCTION THEREOF AND THEIR USE FOR THE PRODUCTION OF MOLDED BODIES, FILAMENTS, FIBERS AND FILMS |
| US4988792A (en) * | 1990-01-19 | 1991-01-29 | General Electric Company | Liquid crystalline polyesteretherimide from a bisimidodiphenol |
| US5173562A (en) * | 1990-10-29 | 1992-12-22 | Chisso America Inc. | Liquid crystal polymer composition containing bisphenol A in combination with 4,4'-thiodiphenol |
-
1994
- 1994-10-20 CN CN94116639A patent/CN1034339C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323097C (en) * | 2002-06-12 | 2007-06-27 | 三菱化学株式会社 | Process for producing polyester resin |
| CN101508897B (en) * | 2009-03-11 | 2011-11-09 | 中山大学 | Novel spinnable thermotropic liquor polyester imide, synthesis and uses thereof |
| CN101560294B (en) * | 2009-05-19 | 2011-11-09 | 中山大学 | Compatible thermotropic liquid crystal polymer and method and application thereof |
| CN106810695A (en) * | 2017-01-12 | 2017-06-09 | 苏州大学 | A kind of aromatic polyesterimides and preparation method thereof |
| CN109825082A (en) * | 2019-02-10 | 2019-05-31 | 成都其其小数科技有限公司 | A kind of polyesterimide/bismaleimide resin composite material and preparation method |
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| Publication number | Publication date |
|---|---|
| CN1034339C (en) | 1997-03-26 |
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