CN105295032B - Long carbon chain semi-aromatic nylon and its synthetic method - Google Patents
Long carbon chain semi-aromatic nylon and its synthetic method Download PDFInfo
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Abstract
The invention discloses a kind of Long carbon chain semi-aromatic nylon and its synthetic method, the Long carbon chain semi-aromatic nylon has following structure shown in formula I：In formula I, a=10~100, b=10~200, c=10~100, d=10~100, R is polyesteramide.Long carbon chain semi-aromatic nylon 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 a kind of Long carbon chain semi-aromatic nylon 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
The Long carbon chain semi-aromatic nylon of a step melt polymerization different and with biological source, can be applied to field of electronics, LED
Field, automotive field, Aero-Space and military industry field etc..
To reach above-mentioned purpose, the present invention uses following scheme：
A kind of Long carbon chain semi-aromatic nylon, it has following structure shown in formula I：
Ⅰ
In formula I, a=10~100, b=10~200, c=10~100, d=10~100, R is polyesteramide, and it has
Such as Formula Il structure：
II
In Formula II, x=10~200, y=10~200, z=10~100；
The Long carbon chain semi-aromatic nylon is formed by monomer 1 and polyesteramide copolymerization, and the monomer 1 is that mol ratio is 1:
0.7~0.99:0.01~0.3 decamethylene diamine, terephthalic acid (TPA) and adipic acid, and the decamethylene diamine and terephthalic acid (TPA) and oneself two
The mol ratio of both consumption sums of acid is 1, and the addition of the polyesteramide is the 1~8% of the gross weight of monomer 1.
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 Long carbon chain semi-aromatic nylon is 0.7~1.0dL/g, glass
Glass temperature Tg>=100 DEG C, melting temperature TmFor 294~305 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 Long carbon chain semi-aromatic nylon, 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 1:0.7~0.99:0.01~0.3 decamethylene diamine, terephthalic acid (TPA),
Adipic acid, and the decamethylene diamine and both terephthalic acid (TPA) and adipic acid consumption and mol ratio be 1, the polyesteramide plus
It is the 1~8% of the gross weight of monomer 1 to enter amount；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, 2,2'- (1,3- phenylenes)-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 polyester acyl
Amine, 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, the acyl of N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene two
Amine.
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 total for the monomer 1
The 0.5~2.5% of weight.
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 adipic acid, while adding polyesteramide to improve the breach of copolymer
Impact strength and antistatic effect, add N, and N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides is handled
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, passes through terminal hydroxy group and the Long carbon chain semi-aromatic nylon of organo montmorillonite
End group reaction, reach regulation molecular weight purpose.Further, since organo montmorillonite has nanometer small-size effect, it can be with
Improve 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 the virtue of Long carbon chain half in melt polymerization process
After the Amino End Group reaction of fragrant race's nylon, 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 Long carbon chain semi-aromatic nylon building-up process, its amide group can be with Long carbon chain semiaromatic
The end group of race's nylon reacts to improve compatibility, and hindered piperidine base can provide antioxidation and improve the dyeing of copolymer
Property.
The present invention compares the advantage of prior art and had the beneficial effect that：
(1) inventor is directed to the defect of existing polyamide 10T resin processing temperature narrow limits, has carried out new tree
The design of fat molecular structure, and the fusing point of copolymer is reduced by adding adipic acid, while adding polyesteramide to improve altogether
The notch impact strength and antistatic effect of polymers, add N, N`- bis- (2,2,6,6- tetramethyl -4- piperidyls) -1,3- benzene two
Acid amides handles the xanthochromia problem in polymerization process.Long carbon chain semi-aromatic nylon of the present invention has higher mechanical property and resistance to
Hot property, low water absorption, processing characteristics is excellent and characteristic with biological source, can be applied to field of electronics, LED necks
Domain, automotive field, Aero-Space and military industry field etc..
(2) method that preparation method of the present invention uses one-step polymerization, it, which has, reduces process, shortens flow, reduces cost,
Put forward large-duty advantage；Preparation technology of the present invention is easy, and polymerization process is easy to operate, is easy to management and control, can be fully achieved institute
It is required that polymerizing condition, facilitate its it is industrialized realize；And in the course of the polymerization process without using any organic solvent, to human body and
Environment is not dangerous, and security is good.
(3) decamethylene diamine used in raw material of the present invention is prepared by the castor oil of nature, therefore, present invention system
The standby Long carbon chain semi-aromatic nylon that obtains is 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 Long carbon chain semi-aromatic nylon of the present invention；
Fig. 2 show the nonisothermal crystallization melting curve figure of the Long carbon chain semi-aromatic nylon 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.
Long carbon chain semi-aromatic nylon of the present invention, it has following structure shown in formula I：
Ⅰ
In formula I, a=10~100, b=10~200, c=10~100, d=10~100, R is polyesteramide, and it has
Such as Formula Il structure：
II
In Formula II, x=10~200, y=10~200, z=10~100.
The reaction mechanism of Long carbon chain semi-aromatic nylon of the present invention is following (synthesis process flow diagram is see Fig. 1)：
Reaction mechanism
It is the Amino End Group of decamethylene diamine, the end carboxyl of terephthalic acid (TPA), the end carboxyl of adipic acid, poly- from above-mentioned reaction equation
The Amino End Group and end carboxyl of esteramides, these groups, which can react to each other, obtains Long carbon chain semi-aromatic Buddhist nun of the present invention
Dragon.
And the reaction mechanism of the polyesteramide added in above-mentioned Long carbon chain semi-aromatic nylon course of reaction is as follows：
Reaction mechanism
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.；
Adipic acid, selected from Shandong Guang Yin new materials 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；
11- aminoundecanoic acids, selected from Taiyuan Zhong Lianze agrochemicals Co., Ltd；
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 Long carbon chain semi-aromatic nylon of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 164.5g (0.99mol) terephthalic acid (TPA),
1.5g (0.01mol) adipic acid is added in stirring-type polymer reactor, while add 1% (3.4g) of the gross weight of monomer 1
Polyesteramide, 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 vacuumize
5min, leads to nitrogen 5min, and so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control stirring-type polymerization is anti-
It is 0.3MPa to answer system pressure in device；
(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 Long carbon chain semi-aromatic nylon of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 116.3g (0.7mol) terephthalic acid (TPA),
43.8g (0.3mol) adipic acid is added in stirring-type polymer reactor, while add 8% (26.6g) of the gross weight of monomer 1
Polyesteramide, 8% (26.6g) organo montmorillonite, 3% (10.0g) benzoic acid, 0.3% (1.0g) N, N`- bis- (2,2,
6,6- tetramethyl -4- piperidyls) -1,3- benzene diamides, add 100mL water as mass-and heat-transfer medium；Then vacuumize
5min, leads to nitrogen 5min, and so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control stirring-type polymerization is anti-
It is 0.2MPa to answer system pressure in device；
(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 Long carbon chain semi-aromatic nylon of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 149.5g (0.9mol) terephthalic acid (TPA),
14.6g (0.1mol) adipic acid is added in stirring-type polymer reactor, while add 2% (6.7g) of the gross weight of monomer 1
Polyesteramide, 0.5% (1.7g) organo montmorillonite, 0.5% (1.7g) 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 vacuumize
5min, leads to nitrogen 5min, and so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control stirring-type polymerization is anti-
It is 0.3MPa to answer system pressure in device；
(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 Long carbon chain semi-aromatic nylon of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 132.9g (0.8mol) terephthalic acid (TPA),
29.2g (0.2mol) adipic acid is added in stirring-type polymer reactor, while add 6% (20.1g) of the gross weight of monomer 1
Polyesteramide, 5% (16.7g) organo montmorillonite, 2.5% (8.4g) 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 vacuumize
5min, leads to nitrogen 5min, and so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control stirring-type polymerization is anti-
It is 0.3MPa to answer system pressure in device；
(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 temperature reaches 215 DEG C, 2.0MPa is deflated to,
And pressure is maintained 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, it is permanent
Temperature is persistently vacuumized 0.3 hour, and 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 Long carbon chain semi-aromatic nylon of the present embodiment, comprises the following steps：
(1) by the monomer 1 after vacuum drying：172.3g (1mol) decamethylene diamine, 144.5g (0.87mol) terephthalic acid (TPA),
19.0g (0.13mol) adipic acid is added in stirring-type polymer reactor, while adding 4% (13.4g) of the gross weight of monomer 1
Polyesteramide, 3% (10.1g) organo montmorillonite, 1.5% (5.0g) 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 vacuumize
5min, leads to nitrogen 5min, and so circulation 6 times makes in the environment that reactant is present under nitrogen protection, control stirring-type polymerization is anti-
It is 0.3MPa to answer system pressure in device；
(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 Long carbon chain semi-aromatic nylon obtained by the present embodiment is as shown in Fig. 2 in figure
The melting peak peak temperature (i.e. melting temperature) for showing the Long carbon chain semi-aromatic nylon is 301.24 DEG C.
Hereinafter list is constituted for the raw material of embodiment 1~5：
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.
Results of property is see following table：
The embodiment performance list of table 2
From table 2 it can be seen that the addition of adipic acid is more, the tensile strength of Long carbon chain semi-aromatic nylon, vitrifying
Transition temperature and melting temperature are lower, and impact strength is higher；The water absorption rate change of each embodiment is little；With molecular weight regulator
The addition of (organo montmorillonite and benzoic acid) increases, and its inherent viscosity diminishes.Wherein, the combination property of embodiment 5 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 (9)
1. a kind of Long carbon chain semi-aromatic nylon, it is characterised in that it has following structure shown in formula I：
In formula I, a=10~100, b=10~200, c=10~100, d=10~100, R is polyesteramide, and it has as follows
Formula II structure：
In Formula II, x=10~200, y=10~200, z=10~100；
The Long carbon chain semi-aromatic nylon is formed by monomer 1 and polyesteramide copolymerization, and the monomer 1 is that mol ratio is 1:0.7
~0.99:0.01~0.3 decamethylene diamine, terephthalic acid (TPA) and adipic acid, and the decamethylene diamine and terephthalic acid (TPA) and adipic acid
The mol ratio of both consumption sums is 1, and the addition of the polyesteramide is the 1~8% of the gross weight of monomer 1.
2. Long carbon chain semi-aromatic nylon according to claim 1, it is characterised in that the addition of the polyesteramide is
The 2~6% of the gross weight of monomer 1.
3. Long carbon chain semi-aromatic nylon according to claim 1, it is characterised in that the Long carbon chain semi-aromatic nylon
Inherent viscosity be 0.7~1.0dL/g, glass transition temperature Tg>=100 DEG C, melting temperature TmFor 294~305 DEG C.
4. Long carbon chain semi-aromatic nylon according to claim 1, it is characterised in that the polyesteramide is total to by monomer 2
Poly- to form, 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.
5. Long carbon chain semi-aromatic nylon according to claim 4, it is characterised in that the polyesteramide is synthesized by following
Method is made：(1) monomer 2 after vacuum drying is added in stirring-type polymer reactor, while adding the monomer 2
0.1~2% titanium compound of gross weight is used as catalyst, addition suitable quantity of water；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, controls the stirring-type
System pressure is 0.1~0.5MPa in polymer 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 Long carbon chain semi-aromatic nylon described in a kind of claim 1, it is characterised in that including following step
Suddenly：
(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 1:0.7~0.99:0.01~0.3 decamethylene diamine, terephthalic acid (TPA), adipic acid, and the decamethylene diamine with
The mol ratio of both terephthalic acid (TPA) and adipic acid consumption sum is 1, and the addition of the polyesteramide is the gross weight of monomer 1
1~8%；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, 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；
The polyesteramide is made by following synthetic method：(1) monomer 2 after vacuum drying is added to stirring-type polymerization
In reactor, while adding 0.1~2% titanium compound of the gross weight of monomer 2 as catalyst, addition suitable quantity of water；So
After vacuumize 3~10min, lead to inert gas 3~10min, so circulate 5~10 times, reactant is present in inert gas guarantor
In environment under shield, it is 0.1~0.5MPa to control system pressure in the stirring-type polymer 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.
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 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 be addition be the gross weight of monomer 1 0.1~0.3% N, N`- bis- (2,2,6,6- tetramethyls-
4- piperidyls) -1,3- benzene diamides.
9. synthetic method according to claim 8, 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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| US4644052A (en) * | 1985-08-15 | 1987-02-17 | Ashland Oil, Inc. | Reaction of bis-oxazoline with polycarboxylic acid catalyzed by alkali or alkaline earth metal cationic complex |
| CN104163918A (en) * | 2013-05-20 | 2014-11-26 | 上海杰事杰新材料(集团)股份有限公司 | High-temperature-resistant nylon PA66T material and preparation method thereof |
| CN104250377A (en) * | 2013-06-25 | 2014-12-31 | 上海杰事杰新材料(集团)股份有限公司 | Low-water absorption biological nylon material PA610T and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5183861A (en) * | 1989-05-23 | 1993-02-02 | Virginia Tech Intellectual Properties, Inc. | Polyalkyloxazoline/polylactone copolymers, processes for making, and uses |
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|---|---|---|---|---|
| US4644052A (en) * | 1985-08-15 | 1987-02-17 | Ashland Oil, Inc. | Reaction of bis-oxazoline with polycarboxylic acid catalyzed by alkali or alkaline earth metal cationic complex |
| CN104163918A (en) * | 2013-05-20 | 2014-11-26 | 上海杰事杰新材料(集团)股份有限公司 | High-temperature-resistant nylon PA66T material and preparation method thereof |
| CN104250377A (en) * | 2013-06-25 | 2014-12-31 | 上海杰事杰新材料(集团)股份有限公司 | Low-water absorption biological nylon material PA610T and preparation method thereof |
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