CN105348520B - Semiaromatic polyamide composition and its synthetic method - Google Patents
Semiaromatic polyamide composition and its synthetic method Download PDFInfo
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- CN105348520B CN105348520B CN201510890781.0A CN201510890781A CN105348520B CN 105348520 B CN105348520 B CN 105348520B CN 201510890781 A CN201510890781 A CN 201510890781A CN 105348520 B CN105348520 B CN 105348520B
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- 239000000203 mixture Substances 0.000 title claims abstract description 45
- 229920006012 semi-aromatic polyamide Polymers 0.000 title claims abstract description 42
- 238000010189 synthetic method Methods 0.000 title claims abstract description 23
- 229920006149 polyester-amide block copolymer Polymers 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 229920000642 polymer Polymers 0.000 claims description 67
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 62
- 239000000178 monomer Substances 0.000 claims description 58
- 229910052757 nitrogen Inorganic materials 0.000 claims description 47
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 44
- 238000006243 chemical reaction Methods 0.000 claims description 34
- -1 propyl titanate Chemical compound 0.000 claims description 26
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims description 24
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 23
- 239000011261 inert gas Substances 0.000 claims description 22
- GUOSQNAUYHMCRU-UHFFFAOYSA-N 11-Aminoundecanoic acid Chemical class NCCCCCCCCCCC(O)=O GUOSQNAUYHMCRU-UHFFFAOYSA-N 0.000 claims description 21
- 238000006116 polymerization reaction Methods 0.000 claims description 17
- 238000007599 discharging Methods 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000002156 mixing Methods 0.000 claims description 15
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 14
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 14
- 238000001291 vacuum drying Methods 0.000 claims description 13
- 239000005711 Benzoic acid Substances 0.000 claims description 12
- 235000010233 benzoic acid Nutrition 0.000 claims description 12
- YQLZOAVZWJBZSY-UHFFFAOYSA-N decane-1,10-diamine Chemical compound NCCCCCCCCCCN YQLZOAVZWJBZSY-UHFFFAOYSA-N 0.000 claims description 12
- 239000000376 reactant Substances 0.000 claims description 12
- 238000002844 melting Methods 0.000 claims description 11
- 230000008018 melting Effects 0.000 claims description 11
- 150000003609 titanium compounds Chemical class 0.000 claims description 9
- 238000010792 warming Methods 0.000 claims description 9
- 238000007334 copolymerization reaction Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 claims description 8
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical class O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 claims description 8
- 229910052786 argon Inorganic materials 0.000 claims description 7
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 claims description 7
- 150000002148 esters Chemical class 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- 239000003963 antioxidant agent Substances 0.000 claims description 6
- 230000003078 antioxidant effect Effects 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 6
- 125000001989 1,3-phenylene group Chemical group [H]C1=C([H])C([*:1])=C([H])C([*:2])=C1[H] 0.000 claims description 5
- 230000009477 glass transition Effects 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims 1
- 235000019253 formic acid Nutrition 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 abstract description 6
- 238000012545 processing Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 description 12
- 230000015572 biosynthetic process Effects 0.000 description 10
- 238000003786 synthesis reaction Methods 0.000 description 9
- 238000012546 transfer Methods 0.000 description 9
- 239000004952 Polyamide Substances 0.000 description 8
- 229920001577 copolymer Polymers 0.000 description 8
- 229920002647 polyamide Polymers 0.000 description 8
- 239000002994 raw material Substances 0.000 description 8
- 238000012360 testing method Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 239000007790 solid phase Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- HMOZDINWBHMBSQ-UHFFFAOYSA-N 2-[3-(4,5-dihydro-1,3-oxazol-2-yl)phenyl]-4,5-dihydro-1,3-oxazole Chemical compound O1CCN=C1C1=CC=CC(C=2OCCN=2)=C1 HMOZDINWBHMBSQ-UHFFFAOYSA-N 0.000 description 4
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 4
- NOKXNDKMAPFVBB-UHFFFAOYSA-N CC(C)[Ti] Chemical compound CC(C)[Ti] NOKXNDKMAPFVBB-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- IMSODMZESSGVBE-UHFFFAOYSA-N 2-Oxazoline Chemical compound C1CN=CO1 IMSODMZESSGVBE-UHFFFAOYSA-N 0.000 description 2
- 229920000106 Liquid crystal polymer Polymers 0.000 description 2
- 239000004977 Liquid-crystal polymers (LCPs) Substances 0.000 description 2
- NQRYJNQNLNOLGT-UHFFFAOYSA-N Piperidine Chemical compound C1CCNCC1 NQRYJNQNLNOLGT-UHFFFAOYSA-N 0.000 description 2
- 239000004734 Polyphenylene sulfide Substances 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 229920006128 poly(nonamethylene terephthalamide) Polymers 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 229920000069 polyphenylene sulfide Polymers 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 125000003504 2-oxazolinyl group Chemical group O1C(=NCC1)* 0.000 description 1
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 244000082204 Phyllostachys viridis Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 229940126678 chinese medicines Drugs 0.000 description 1
- 210000001072 colon Anatomy 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 229920006147 copolyamide elastomer Polymers 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- JBFHTYHTHYHCDJ-UHFFFAOYSA-N gamma-caprolactone Chemical compound CCC1CCC(=O)O1 JBFHTYHTHYHCDJ-UHFFFAOYSA-N 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- SXJVFQLYZSNZBT-UHFFFAOYSA-N nonane-1,9-diamine Chemical compound NCCCCCCCCCN SXJVFQLYZSNZBT-UHFFFAOYSA-N 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920006111 poly(hexamethylene terephthalamide) Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- MHSKRLJMQQNJNC-UHFFFAOYSA-N terephthalamide Chemical compound NC(=O)C1=CC=C(C(N)=O)C=C1 MHSKRLJMQQNJNC-UHFFFAOYSA-N 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/36—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino acids, polyamines and polycarboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/44—Polyester-amides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/48—Polymers modified by chemical after-treatment
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/34—Heterocyclic compounds having nitrogen in the ring
- C08K5/3412—Heterocyclic compounds having nitrogen in the ring having one nitrogen atom in the ring
- C08K5/3432—Six-membered rings
- C08K5/3435—Piperidines
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- General Chemical & Material Sciences (AREA)
- Polyamides (AREA)
Abstract
The present invention relates to a kind of semiaromatic polyamide composition and its synthetic method.The semiaromatic polyamide composition has such as following formula I structure：In Formulas I, a=10~200, b=10~200, c=10~100, R is polyesteramide.Semiaromatic polyamide composition of the present invention has higher a mechanical property and heat resistance, low water absorption, and processing characteristics is excellent and characteristic with biological source, can be applied to field of electronics, LED field, automotive field, Aero-Space and military industry field etc..
Description
Technical field
The present invention relates to Material Field, more particularly to semiaromatic polyamide composition and its synthetic method.
Background technology
In recent years, in order to meet the requirement in the higher performance in the fields such as electronics, electrical equipment, automobile, in particular with surface
The development of mounting technique (Surface Mount Technology, abbreviation SMT), common thermostability engineering plastic polyphenylene sulfide
And the heat resistance of liquid crystal polymer (LCP) can not fully meet its requirement, therefore the higher engineering of exploitation heat resistance (PPS)
Plastics just turn into inevitable.
Semiaromatic polyamide composition is typically by aliphatic diamines or diacid and diacid or diamines with aromatic rings, through polycondensation
And be made, due to having imported aromatic rings on polyamide molecule main chain, its heat resistance and mechanical property are improved, and inhale
Water rate is reduced, and with preferable superiority of effectiveness, it is mainly used in automobile and electric and electronic industry.Industrialized semiaromatic
Polyamide mainly has polyamide 6 T (copolymer), polyamide 9T, polyamide 10T etc..But, the fusing point of polyamide 10T resins
For 320 DEG C or so, it is more or less the same with decomposition temperature, and processing temperature narrow limits easily cause polymer in process
Decompose, so generally reducing its melting temperature using the method with other copolyamides.
Solid phase (Solid state Polymerization) refers to solid (or crystalline phase) monomer below its fusing point
The polymerisation of generation, or the polymerization carried out more than monomer fusing point but below the melting temperature of the polymer of formation are anti-
Should.Due to general 15~30 DEG C of progress below the fusing point of prepolymer of solid phase, its reaction rate relatively slow, reaction time compared with
It is long, and the production process of solid phase is more, flow complicated, requires higher to device parameter, and reaction also needs to ensure functional group
Proportioning close to 1:1, the thickening stage needs vacuum or air-flow to accelerate the discharge of small molecular by product, so as to improve polycondensation production
The molecular weight of thing, therefore, conditions above limit the large-scale promotion of solid phase.Melt polymerization (Melt
Polymerization the polymerization process that monomer and polymer are under molten condition) is referred to, this method process route is simple,
Can continuously it produce, can also Batch Process.Reaction needs to carry out at high temperature, and the reaction time is shorter, and the pair such as hydrone
Product discharge is easy.At present, some researchs, such as Chinese patent have been done in the synthesis in the prior art to semiaromatic polyamide composition
CN102153741A disclose a kind of homopolymer of Long carbon chain semiaromatic heat resistant polyamide and the synthetic method of copolymer and its
Obtained polymerizate, the polymerizate is mainly obtained by the method for solid phase；Chinese patent CN103360599A is public
A kind of semi-aromatic and fatty polyamide block copolymer are opened, the molar percentage of wherein semiaromatic polyamide composition block contains
Amount is that 40%~99%, mole percent level of fatty polyamide block is 1~60%, and the polymerizate, which is mainly, to be passed through
The method of solid phase is obtained；Chinese patent CN101948619A discloses a kind of poly-paraphenylene terephthalamide's nonamethylene diamine material and its system
Preparation Method；Chinese patent CN1106842A discloses polyamide 9T, 9M-T and preparation method thereof.
The content of the invention
It is an object of the invention to provide a kind of higher mechanical property and heat resistance, low water absorption, processing characteristics is excellent
Semiaromatic polyamide composition different and with biological source, can be applied to field of electronics, LED field, automotive field, aviation
Space flight and military industry field etc..
To reach above-mentioned purpose, the present invention uses following scheme：
A kind of semiaromatic polyamide composition, it has such as following formula I structure：
In Formulas I, a=10~200, b=10~200, c=10~100, R is polyesteramide, and it has such as Formula Il knot
Structure：
In Formula II, x=10~200, y=10~200, z=10~100；
The semiaromatic polyamide composition is formed by monomer 1 and polyesteramide copolymerization, and the monomer 1 is that mol ratio is 1:1:
0.05~0.2 decamethylene diamine, terephthalic acid (TPA), 11- aminoundecanoic acids, the polyesteramide addition are the gross weight of monomer 1
The 1~8% of amount.
In wherein some embodiments, the addition of the polyesteramide is the 2~6% of the gross weight of monomer 1.
In wherein some embodiments, the inherent viscosity of the semiaromatic polyamide composition is 0.7~1.0dL/g, vitrifying
Temperature Tg>=100 DEG C, melting temperature TmFor 295~305 DEG C.
In wherein some embodiments, the polyesteramide is formed by the copolymerization of monomer 2, and the monomer 2 is that mol ratio is 1:
0.5~1:0.1~0.4 11- aminoundecanoic acids, 6- caprolactones and 2,2'- (1,3- phenylenes)-bisoxazoline.
In wherein some embodiments, the polyesteramide is made by following synthetic method：(1) by the institute after vacuum drying
State monomer 2 to be added in stirring-type polymer reactor, while 0.1~2% titanium compound for adding the gross weight of monomer 2 is made
For catalyst, add suitable quantity of water (medium of mass-and heat-transfer)；Then 3~10min is vacuumized, leads to 3~10min of inert gas, such as
This circulation 5~10 times, makes in the environment that reactant is present under inert gas shielding, controls in the stirring-type polymer reactor
System pressure is 0.1~0.5MPa；
(2) by the stirring-type polymer reactor airtight heating to 240~260 DEG C, the stirring-type polymerisation is adjusted
The mixing speed of device is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 210 DEG C, it is deflated to
1.6MPa, and maintain pressure in 1.6MPa, after reacting 0.5~4 hour, normal pressure is deflated to, continues to react at 240~260 DEG C
After 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas；The titanium compound is butyl titanate, isopropyl titanium
One or more kinds of mixtures in acid esters, propyl titanate, acrylic titanate esters.
It is a further object of the present invention to provide the synthetic method of above-mentioned semiaromatic polyamide composition, comprise the following steps：
(1) monomer 1 is added in stirring-type polymer reactor, adjusted while adding the polyesteramide, molecular weight
Save agent, antioxidant, water (medium of mass-and heat-transfer)；Then 3~10min is vacuumized, leads to 3~10min of inert gas, so circulation
5~10 times, make in the environment that reactant is present under inert gas shielding, control system pressure in the stirring-type polymer reactor
Power is 0.1~0.5MPa；The monomer 1 is that mol ratio is 1:1:0.05~0.2 decamethylene diamine, terephthalic acid (TPA), 11- amino ten
One acid, the polyesteramide addition is the 1~8% of the addition gross weight of monomer 1；The polyesteramide is by the copolymerization of monomer 2
Form, the monomer 2 is that mol ratio is 1:0.5~1:0.1~0.4 11- aminoundecanoic acids, 6- caprolactones, 2,2'- (1,3-
Phenylene)-bisoxazoline；
(2) by the stirring-type polymer reactor airtight heating to 270~285 DEG C, the stirring-type polymerisation is adjusted
The mixing speed of device is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 215 DEG C, it is deflated to
2.0MPa, and maintain pressure in 2.0MPa, after reacting 0.5~4 hour, normal pressure is deflated to, while being warming up at 306~325 DEG C
Continue after reacting 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas.
Logical inert gas purpose is to reduce the probability that side reaction occurs before reaction；The purpose vacuumized in course of reaction is handle
The water produced in polymerisation is removed, and is conducive to polymerisation forward direction progress.
In wherein some embodiments, above-mentioned synthetic method comprises the following steps：
(1) monomer 1 after vacuum drying is added in stirring-type polymer reactor, while adding the polyamide
Ester, molecular weight regulator, antioxidant, water；Then 4~6min is vacuumized, leads to 4~6min of nitrogen, is so circulated 5~7 times, is made anti-
Answer in the environment that thing is present under nitrogen protection, it is 0.2~0.3MPa to control system pressure in the stirring-type polymer reactor；
(2) in 2~4 hours by the closed constant-speed heating of stirring-type polymer reactor to 272~280 DEG C, adjust institute
The mixing speed for stating stirring-type polymer reactor is 30~50r/min, wherein, when the stirring-type polymer reactor temperature reaches
At 215 DEG C, 2.0MPa is deflated to, and maintains pressure in 2.0MPa, after reacting 1~2 hour, normal pressure is deflated to, is warming up to simultaneously
Continue at 310~320 DEG C after reacting 1~2 hour, constant temperature is persistently vacuumized 0.3~1 hour, and reaction terminates, supplemented in discharging
Nitrogen.
In wherein some embodiments, the polyesteramide is made by following synthetic method：(1) by the institute after vacuum drying
State monomer 2 to be added in stirring-type polymer reactor, while 0.1~2% titanium compound for adding the gross weight of monomer 2 is made
For catalyst, add suitable quantity of water；Then 3~10min is vacuumized, leads to 3~10min of inert gas, so circulates 5~10 times, makes
Reactant is present in the environment under inert gas shielding, control in the stirring-type polymer reactor system pressure be 0.1~
0.5MPa；
(2) by the stirring-type polymer reactor airtight heating to 240~260 DEG C, the stirring-type polymerisation is adjusted
The mixing speed of device is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 210 DEG C, it is deflated to
1.6MPa, and maintain pressure in 1.6MPa, after reacting 0.5~4 hour, normal pressure is deflated to, continues to react at 240~260 DEG C
After 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas；The titanium compound is butyl titanate, isopropyl titanium
One or more kinds of mixtures in acid esters, propyl titanate, acrylic titanate esters.
In wherein some embodiments, the molecular weight regulator be addition be the gross weight of monomer 1 0.1~
8% organo montmorillonite and addition is 0.1~3% benzoic acid of the gross weight of monomer 1；The antioxidant is to add
Measure as 0.1~0.3% N of the gross weight of monomer 1, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides.
In wherein some embodiments, the addition of the polyesteramide is the 2~6% of the gross weight of monomer 1；It is described
The addition of organo montmorillonite is the 0.5~5% of the gross weight of monomer 1, and the addition of the benzoic acid is the gross weight of monomer 1
0.5~2.5%.
The principle of the present invention is as follows：
In order to solve the defect of polyamide 10T resin processing temperature narrow limits, the present invention has carried out new molecular resin knot
The design of structure, the fusing point of copolymer is reduced by adding 11- aminoundecanoic acids, while adding polyesteramide to improve copolymer
Notch impact strength and antistatic effect, add N, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides
To handle the xanthochromia problem in polymerization process.
Polyesteramide has ether epoxide, and it can be combined with free electric charge, and electric charge can be in the way of combination
It is mobile, ionic conduction release electrostatic lotus is carried out along polyesteramide backbone, so as to reach anlistatig effect.Further, since ether oxygen
The bond angle of key is larger, and segment compliance preferably, therefore can improve the notch impact strength of copolymer.
Organo montmorillonite belongs to polyhydroxy inorganic matter, terminal hydroxy group and the end of semiaromatic polyamide composition by organo montmorillonite
Base reacts, and reaches the purpose of regulation molecular weight.Further, since organo montmorillonite has nanometer small-size effect, it can be improved
The modulus and anti-flammability of copolymer, reduction shrinkage factor and water absorption rate.
Benzoic acid belongs to the organic matter of simple function group, the end carboxyl of benzoic acid and semiaromatic adoption in melt polymerization process
After the Amino End Group reaction of acid amides, it no longer carries out the reaction of chain growth, so as to play a part of adjusting molecular weight.
The fusing point of N, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides is 272 DEG C, boiling point>360
DEG C, the better heat stability in semiaromatic polyamide composition building-up process, its amide group can be with semiaromatic polyamide composition
End group reacts to improve compatibility, and hindered piperidine base can provide antioxidation and improve the dyeability of copolymer.
Compared with prior art, the invention has the advantages that：
(1) present invention is directed to the defect of existing polyamide 10T resin processing temperature narrow limits, has carried out new molecular resin
The design of structure, the fusing point of copolymer is reduced by adding 11- aminoundecanoic acids, while adding polyesteramide to improve copolymerization
The notch impact strength and antistatic effect of thing, add N, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls)-acyl of 1,3- benzene two
Amine handles the xanthochromia problem in polymerization process, and gained semiaromatic polyamide composition has higher mechanical property and heat resistance,
Low water absorption, processing characteristics is excellent and characteristic with biological source, can be applied to field of electronics, LED field, automobile
Field, Aero-Space and military industry field etc..
(2) method that synthetic method of the invention uses one-step polymerization, it, which has, reduces process, shortens flow, drops
Low cost, improves the advantage of productivity ratio, and preparation technology is easy, and polymerization process is easy to operate, is easy to management and control, can fully reach
To required polymerizing condition, facilitate its industrialized realization；And in the course of the polymerization process without using any organic solvent, to people
Body and environment are not dangerous, and security is good.
(3) decamethylene diamine used in the present invention, 11- aminoundecanoic acids are prepared by the castor oil of nature, therefore,
The present invention prepares semiaromatic polyamide composition for a kind of bio-based materials, the characteristic with environmental protection.
Brief description of the drawings
Fig. 1 show the synthesis process flow diagram of semiaromatic polyamide composition of the present invention；
Fig. 2 show the nonisothermal crystallization melting curve figure of the semiaromatic polyamide composition of the gained of the embodiment of the present invention 5.
Embodiment
For the feature, technological means and the specific purposes reached, function of the present invention can be further appreciated that, this hair is parsed
Bright advantage and spirit, by following examples, the present invention is further elaborated.
Semiaromatic polyamide composition of the present invention, it has such as following formula I structure：
In Formulas I, a=10~200, b=10~200, c=10~100, R is polyesteramide, and it has such as Formula Il knot
Structure：
In Formula II, x=10~200, y=10~200, z=10~100；
The reaction mechanism of semiaromatic polyamide composition of the present invention is following (synthesis process flow diagram is see Fig. 1)：
From above-mentioned reaction equation, the Amino End Group of decamethylene diamine, the end carboxyl of terephthalic acid (TPA), the end of 11- aminoundecanoic acids
Amino and end carboxyl, the Amino End Group and end carboxyl of polyesteramide, these groups, which can react to each other, obtains of the present invention half
Aromatic polyamide.
And the reaction mechanism of the polyesteramide added in above-mentioned semiaromatic polyamide composition course of reaction is as follows：
After above-mentioned reaction equation, 6- caprolactone open loops its ester group, the Amino End Group of 11- aminoundecanoic acids, 2,2'- (1,
3- phenylenes)-bisoxazoline oxazoline group, these three groups, which can react to each other, obtains the polyester acyl that is added of the present invention
Amine, the inherent viscosity for the polyesteramide that the present invention is added is 0.7~1.0dL/g, glass transition temperature Tg>=80 DEG C, melting temperature
TmFor 215~225 DEG C.
Raw material is as follows used in the embodiment of the present invention：
Decamethylene diamine, selected from Wuxi Yinda Nylon Co., Ltd.；
Terephthalic acid (TPA), selected from Beijing Yanshan Petrochemical Co.；
11- aminoundecanoic acids, selected from Taiyuan Zhong Lianze agrochemicals Co., Ltd；
6- caprolactones in polyesteramide, self-control, raw material, selected from the chemical Science and Technology Ltd. of the rich bamboo grove in Wuhan；
2,2'- (1,3- phenylene)-bisoxazolines, selected from Nanjing colon medication chemistry Co., Ltd；
Butyl titanate, selected from Chemical Reagent Co., Ltd., Sinopharm Group；
Organo montmorillonite, selected from Zhejiang Fenghong New Material Co., Ltd.；
Benzoic acid, selected from Chemical Reagent Co., Ltd., Sinopharm Group；
N, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, has selected from Chinese medicines group chemical reagent
Limit company.
The present invention is described in detail below in conjunction with specific embodiment.
Polyesteramide in following examples is disliked by 11- aminoundecanoic acids, 6- caprolactones, 2,2'- (1,3- phenylenes)-two
Oxazoline copolymerization is formed, and 11- aminoundecanoic acids, 6- caprolactones, the mol ratio of 2,2'- (1,3- phenylene)-bisoxazoline are 1:0.5
~1:0.1~0.4.
Synthetic method is as follows：
(1) by the monomer 2 after vacuum drying：11- aminoundecanoic acids, 6- caprolactones, 2,2'- (1,3- phenylenes)-two are disliked
Oxazoline is added in stirring-type polymer reactor by above-mentioned mol ratio, while adding 0.1~2% titanizing of the gross weight of monomer 2
Compound is used as medium of the appropriate water of catalyst, addition as mass-and heat-transfer；Then 3~10min is vacuumized, leads to inert gas 3
~10min, so circulates 5~10 times, makes in the environment that reactant is present under inert gas shielding, and control stirring-type polymerization is anti-
It is 0.1~0.5MPa to answer system pressure in device；
(2) by stirring-type polymer reactor airtight heating to 240~260 DEG C, the stirring of stirring-type polymer reactor is adjusted
Speed is 0~100r/min, wherein, when stirring-type polymer reactor temperature reaches 210 DEG C, 1.6MPa is deflated to, and maintain
Pressure after reacting 0.5~4 hour, is deflated to normal pressure in 1.6MPa, continues at 240~260 DEG C after reacting 0.5~4 hour,
Constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas；The titanium compound is butyl titanate, isopropyl titanium
One or more kinds of mixtures in acid esters, propyl titanate, acrylic titanate esters.
Embodiment 1
The raw material of polyesteramide used in the present embodiment is constituted and synthesis step is as follows：
(1) by the monomer 2 after vacuum drying：1006.6g (5mol) 11- aminoundecanoic acids, 456.6g (4mol) 6- are in oneself
Ester, 270.3g (1.25mol) 2,2'- (1,3- phenylene)-bisoxazoline are added in stirring-type polymer reactor, are added simultaneously
1% butyl titanate (17.3g) of the gross weight of monomer 2 as catalyst, add 500mL water as mass-and heat-transfer medium；
Then 5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control is stirred
It is 0.2MPa to mix system pressure in formula polymer reactor；
(2) in 2.5 hours by the closed constant-speed heating of stirring-type polymer reactor to 250 DEG C, regulation stirring-type polymerization is anti-
The mixing speed for answering device is 40r/min, wherein, when stirring-type polymer reactor temperature reaches 210 DEG C, 1.6MPa is deflated to,
And maintain pressure in 1.6MPa, after reacting 1.5 hours, normal pressure is deflated to, is continued at 250 DEG C after reacting 1.5 hours, constant temperature is held
Continuous to vacuumize 0.5 hour, reaction terminates, and nitrogen is supplemented in discharging.
A kind of synthetic method of semiaromatic polyamide composition of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 166.1g (1mol) terephthalic acid (TPA),
10.1g (0.05mol) 11- aminoundecanoic acids are added in stirring-type polymer reactor, while adding the 1% of the gross weight of monomer 1
The polyesteramide of (3.5g), 0.1% (0.3g) organo montmorillonite, 0.1% (0.3g) benzoic acid, 0.1% (0.3g) N, N
`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then
5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that reactant is present under nitrogen protection, controls stirring-type
System pressure is 0.3MPa in polymer reactor；
(2) in 4 hours by the closed constant-speed heating of stirring-type polymer reactor to 285 DEG C, adjust stirring-type polymerisation
The mixing speed of device is 40r/min, wherein, when stirring-type polymer reactor temperature reaches 215 DEG C, 2.0MPa is deflated to, and
Pressure is maintained in 2.0MPa, after reaction 0.5 hour, normal pressure is deflated to, while after being warming up at 325 DEG C and continuing to react 0.5 hour,
Constant temperature is persistently vacuumized 2 hours, and reaction terminates, and nitrogen is supplemented in discharging.
Embodiment 2
The raw material of polyesteramide used is constituted and synthesis step be the same as Example 1 in the present embodiment.
A kind of synthetic method of semiaromatic polyamide composition of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 166.1g (1mol) terephthalic acid (TPA),
40.3g (0.2mol) 11- aminoundecanoic acids are added in stirring-type polymer reactor, while adding the 8% of single 1 gross weight
The polyesteramide of (30.3g), 8% (30.3g) organo montmorillonite, 3% (11.4g) benzoic acid, 0.3% (1.1g) N, N
`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then
5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that stirring-type polymer reactor is present under nitrogen protection,
It is 0.2MPa to control system pressure in stirring-type polymer reactor；
(2) in 2 hours by the closed constant-speed heating of stirring-type polymer reactor to 270 DEG C, adjust stirring-type polymerisation
The mixing speed of device is 40r/min, wherein, when stirring-type polymer reactor temperature reaches 215 DEG C, 2.0MPa is deflated to, and
Pressure is maintained in 2.0MPa, after reaction 4 hours, normal pressure is deflated to, while after being warming up at 306 DEG C and continuing to react 4 hours, constant temperature
Persistently vacuumize 0.1 hour, reaction terminates, nitrogen is supplemented in discharging.
Embodiment 3
The raw material of polyesteramide used is constituted and synthesis step be the same as Example 1 in the present embodiment.
A kind of synthetic method of semiaromatic polyamide composition of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 166.1g (1mol) terephthalic acid (TPA),
20.1g (0.1mol) 11- aminoundecanoic acids are added in stirring-type polymer reactor, while adding the 2% of single 1 gross weight
The polyesteramide of (7.2g), 0.5% (1.8g) organo montmorillonite, 0.5% (1.8g) benzoic acid, 0.2% (0.7g) N, N
`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then
5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that reactant is present under nitrogen protection, controls stirring-type
System pressure is 0.3MPa in polymer reactor；
(2) in 3.5 hours by the closed constant-speed heating of stirring-type polymer reactor to 280 DEG C, regulation stirring-type polymerization is anti-
The mixing speed for answering device is 40r/min, wherein, when stirring-type polymer reactor temperature reaches 215 DEG C, 2.0MPa is deflated to,
And pressure is maintained in 2.0MPa, after reaction 1 hour, normal pressure is deflated to, while after being warming up at 320 DEG C and continuing to react 1 hour, it is permanent
Temperature is persistently vacuumized 1 hour, and reaction terminates, and nitrogen is supplemented in discharging.
Embodiment 4
The raw material of polyesteramide used is constituted and synthesis step be the same as Example 1 in the present embodiment.
A kind of synthetic method of semiaromatic polyamide composition of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 166.1g (1mol) terephthalic acid (TPA),
30.2g (0.15mol) 11- aminoundecanoic acids are added in stirring-type polymer reactor, while adding the 6% of the amount of monomer 1
The polyesteramide of (22.1g), 5% (18.4g) organo montmorillonite, 2.5% (9.2g) benzoic acid, 0.2% (0.7g) N, N
`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then
5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that reactant is present under nitrogen protection, controls stirring-type
System pressure is 0.3MPa in polymer reactor；
(2) in 2.5 hours by the closed constant-speed heating of stirring-type polymer reactor to 272 DEG C, regulation stirring-type polymerization is anti-
The mixing speed for answering device is 40r/min, wherein, when stirring-type polymer reactor reaches 215 DEG C, 2.0MPa is deflated to, and tie up
Pressure is held in 2.0MPa, after reaction 2 hours, normal pressure is deflated to, while after being warming up at 310 DEG C and continuing to react 2 hours, constant temperature is held
Continuous to vacuumize 0.3 hour, reaction terminates, and nitrogen is supplemented in discharging.
Embodiment 5
The raw material of polyesteramide used is constituted and synthesis step be the same as Example 1 in the present embodiment.
A kind of synthetic method of semiaromatic polyamide composition of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 166.1g (1mol) terephthalic acid (TPA),
20.1g (0.1mol) 11- aminoundecanoic acids are added in stirring-type polymer reactor, while adding the 4% of single 1 gross weight
The polyesteramide of (14.3g), 3% (10.8g) organo montmorillonite, 1.5% (5.4g) benzoic acid, 0.2% (0.7g) N, N
`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then
5min is vacuumized, leads to nitrogen 5min, so circulation 6 times makes in the environment that reactant is present under nitrogen protection, controls stirring-type
System pressure is 0.3MPa in polymer reactor；
(2) in 3 hours by the closed constant-speed heating of stirring-type polymer reactor to 275 DEG C, adjust stirring-type polymerisation
The mixing speed of device is 40r/min, wherein, when stirring-type polymer reactor temperature reaches 215 DEG C, 2.0MPa is deflated to, and
Pressure is maintained in 2.0MPa, after reaction 1.5 hours, normal pressure is deflated to, while after being warming up at 315 DEG C and continuing to react 1.5 hours,
Constant temperature is persistently vacuumized 0.5 hour, and reaction terminates, and nitrogen is supplemented in discharging.
The nonisothermal crystallization melting curve figure of semiaromatic polyamide composition obtained by the present embodiment in figure as shown in Fig. 2 show
The melting peak peak temperature (i.e. melting temperature) of the semiaromatic polyamide composition is 302.19 DEG C.
It is embodiment list below：
The embodiment raw material of table 1 constitutes list
The made sample of above-described embodiment is subjected to following performance test：
Tensile property：By GB/T1040-2006 standard testings, rate of extension 50mm/min；
Impact property：By GB/T1843-2008 standard testings, batten thickness is 3.2mm；
Water absorption rate：By GB/T1034-2008 standard testings, thickness of test piece 2mm；
Inherent viscosity：By GB/T1632-2008 standard testings, the solvent concentrated sulfuric acid；
Glass transition temperature：By GB/T19466.2-2004 standard testings；
Melting temperature：By GB/T19466.3-2004 standard testings.
The embodiment performance list of table 2
As can be seen from the above embodiments, the addition of 11- aminoundecanoic acids is more, and the stretching of semiaromatic polyamide composition is strong
Degree, glass transition temperature and melting temperature are lower, and impact strength is higher；The water absorption rate change of each embodiment is little；With point
The addition of son amount conditioning agent (organo montmorillonite and benzoic acid) increases, and its inherent viscosity diminishes.Wherein, the synthesis of embodiment 5
Performance is optimal.
Each technical characteristic of embodiment described above can be combined arbitrarily, to make description succinct, not to above-mentioned reality
Apply all possible combination of each technical characteristic in example to be all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, the scope of this specification record is all considered to be.
Embodiment described above only expresses the several embodiments of the present invention, and it describes more specific and detailed, but simultaneously
Can not therefore it be construed as limiting the scope of the patent.It should be pointed out that coming for one of ordinary skill in the art
Say, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to the protection of the present invention
Scope.Therefore, the protection domain of patent of the present invention should be determined by the appended claims.
Claims (10)
1. a kind of semiaromatic polyamide composition, it is characterised in that it has such as following formula I structure：
In Formulas I, a=10~200, b=10~200, c=10~100, R is polyesteramide, and it has such as Formula Il structure：
In Formula II, x=10~200, y=10~200, z=10~100；
The semiaromatic polyamide composition is formed by monomer 1 and polyesteramide copolymerization, and the monomer 1 is that mol ratio is 1:1:0.05~
0.2 decamethylene diamine, terephthalic acid (TPA), 11- aminoundecanoic acids, the addition of the polyesteramide are the 1 of the gross weight of monomer 1
~8%.
2. semiaromatic polyamide composition according to claim 1, it is characterised in that the addition of the polyesteramide is described
The 2~6% of the gross weight of monomer 1.
3. semiaromatic polyamide composition according to claim 1, it is characterised in that the characteristic of the semiaromatic polyamide composition is glued
Spend for 0.7~1.0dL/g, glass transition temperature Tg>=100 DEG C, melting temperature TmFor 295~305 DEG C.
4. semiaromatic polyamide composition according to claim 1, it is characterised in that the polyesteramide by the copolymerization of monomer 2 and
Into the monomer 2 is that mol ratio is 1:0.5~1:(1,3- is sub- by 0.1~0.4 11- aminoundecanoic acids, 6- caprolactones and 2,2'-
Phenyl)-bisoxazoline.
5. semiaromatic polyamide composition according to claim 4, it is characterised in that the polyesteramide is by following synthetic method
It is made：(1) monomer 2 after vacuum drying is added in stirring-type polymer reactor, while adding the gross weight of monomer 2
0.1~2% titanium compound of amount is used as catalyst, addition suitable quantity of water；Then 3~10min is vacuumized, logical inert gas 3~
10min, so circulates 5~10 times, makes in the environment that reactant is present under inert gas shielding, controls the stirring-type polymerization
System pressure is 0.1~0.5MPa in reactor；
(2) by the stirring-type polymer reactor airtight heating to 240~260 DEG C, the stirring-type polymer reactor is adjusted
Mixing speed is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 210 DEG C, it is deflated to
1.6MPa, and maintain pressure in 1.6MPa, after reacting 0.5~4 hour, normal pressure is deflated to, continues to react at 240~260 DEG C
After 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas；The titanium compound is butyl titanate, isopropyl metatitanic acid
One or more kinds of mixtures in ester, propyl titanate, acrylic titanate esters.
6. the synthetic method of the semiaromatic polyamide composition described in a kind of claim 1, it is characterised in that comprise the following steps：
(1) monomer 1 is added in stirring-type polymer reactor, at the same add the polyesteramide, molecular weight regulator,
Antioxidant, water；Then 3~10min is vacuumized, leads to 3~10min of inert gas, so circulates 5~10 times, there is reactant
In the environment under inert gas shielding, it is 0.1~0.5MPa to control system pressure in the stirring-type polymer reactor；It is described
Monomer 1 is that mol ratio is 1:1:0.05~0.2 decamethylene diamine, terephthalic acid (TPA), 11- aminoundecanoic acids, the polyesteramide add
Enter amount to add the 1~8% of the gross weight of monomer 1；The polyesteramide is formed by the copolymerization of monomer 2, the monomer 2 for mole
Than for 1:0.5~1:0.1~0.4 11- aminoundecanoic acids, 6- caprolactones, 2,2'- (1,3- phenylenes)-bisoxazoline；
(2) by the stirring-type polymer reactor airtight heating to 270~285 DEG C, the stirring-type polymer reactor is adjusted
Mixing speed is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 215 DEG C, it is deflated to
2.0MPa, and maintain pressure in 2.0MPa, after reacting 0.5~4 hour, normal pressure is deflated to, while being warming up at 306~325 DEG C
Continue after reacting 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas.
7. synthetic method according to claim 6, it is characterised in that comprise the following steps：
(1) monomer 1 after vacuum drying is added in stirring-type polymer reactor, at the same add the polyesteramide,
Molecular weight regulator, antioxidant, water；Then 4~6min is vacuumized, leads to 4~6min of nitrogen, so circulates 5~7 times, makes reaction
Thing is present in the environment under nitrogen protection, and it is 0.2~0.3MPa to control system pressure in the stirring-type polymer reactor；
(2) in 2~4 hours by the closed constant-speed heating of stirring-type polymer reactor to 272~280 DEG C, regulation described in stir
The mixing speed for mixing formula polymer reactor is 30~50r/min, wherein, when the stirring-type polymer reactor temperature reaches 215
DEG C when, be deflated to 2.0MPa, and maintain pressure in 2.0MPa, after reaction 1~2 hour, normal pressure be deflated to, while being warming up to 310
Continue at~320 DEG C after reacting 1~2 hour, constant temperature is persistently vacuumized 0.3~1 hour, and reaction terminates, nitrogen is supplemented in discharging
Gas.
8. the synthetic method according to claim 6 or 7, it is characterised in that the polyesteramide is by following synthetic method system
：(1) monomer 2 after vacuum drying is added in stirring-type polymer reactor, while adding the gross weight of monomer 2
0.1~2% titanium compound be used as catalyst, add suitable quantity of water；Then 3~10min is vacuumized, logical inert gas 3~
10min, so circulates 5~10 times, makes in the environment that reactant is present under inert gas shielding, controls the stirring-type polymerization
System pressure is 0.1~0.5MPa in reactor；
(2) by the stirring-type polymer reactor airtight heating to 240~260 DEG C, the stirring-type polymer reactor is adjusted
Mixing speed is 0~100r/min, wherein, when the stirring-type polymer reactor temperature reaches 210 DEG C, it is deflated to
1.6MPa, and maintain pressure in 1.6MPa, after reacting 0.5~4 hour, normal pressure is deflated to, continues to react at 240~260 DEG C
After 0.5~4 hour, constant temperature is persistently vacuumized 0.1~2 hour, and reaction terminates, the topping up in discharging；
In above-mentioned steps, the inert gas is nitrogen or argon gas；The titanium compound is butyl titanate, isopropyl metatitanic acid
One or more kinds of mixtures in ester, propyl titanate, acrylic titanate esters.
9. the synthetic method according to claim 6 or 7, it is characterised in that the molecular weight regulator is that addition is institute
0.1~8% organo montmorillonite and addition for stating the gross weight of monomer 1 are 0.1~3% benzene of the gross weight of monomer 1
Formic acid；The antioxidant is 0.1~0.3% N that addition is the gross weight of the monomer 1, (2,2,6,6- tetramethyl -4- piperazines of N`- bis-
Piperidinyl) -1,3- benzenedicarboxamides.
10. synthetic method according to claim 9, it is characterised in that the addition of the polyesteramide is the monomer 1
The 2~6% of gross weight；The addition of the organo montmorillonite is the 0.5~5% of the gross weight of monomer 1, the benzoic acid
Addition is the 0.5~2.5% of the gross weight of monomer 1.
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