CN113698590B - Melt-processable end-capped fluorine-containing polyarylether resin as well as preparation method and application thereof - Google Patents
Melt-processable end-capped fluorine-containing polyarylether resin as well as preparation method and application thereof Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及高分子材料技术领域,尤其涉及一种可熔融加工封端含氟聚芳醚树脂及其制备方法和应用。The invention relates to the technical field of polymer materials, in particular to a melt-processable end-capped fluorine-containing polyarylene ether resin and a preparation method and application thereof.
背景技术Background technique
含氟聚芳醚中存在大量的C-F键和芳环结构,使其通常具有良好的溶解性、热稳定性、光学性能、低表面能、低摩擦系数、低介电常数和耐化学腐蚀性等优异的性能,因此含十氟联氟的聚芳醚材料在高性能涂料、燃料电池、复合材料和光学材料等领域得到了广泛的应用,其中,十氟联苯单体因其极高的含氟量常被应用到高分子材料中。There are a large number of C-F bonds and aromatic ring structures in fluorinated polyarylene ethers, which make them usually have good solubility, thermal stability, optical properties, low surface energy, low friction coefficient, low dielectric constant and chemical resistance, etc. Due to its excellent performance, the polyarylene ether materials containing decafluorobifluorine have been widely used in the fields of high-performance coatings, fuel cells, composite materials and optical materials. Fluorine content is often used in polymer materials.
对于传统热塑性树脂而言,熔融加工是体型材料成型加工的重要手段之一。然而采用十氟联苯单体制备的聚合物因其单体十个氟原子都具有反应活性,在聚合反应过程及高温加工过程中极易与聚合反应残留的活性端基反应,产生支化、交联等结构,影响熔体流动性和稳定性,不利于熔融加工构筑体型材料。因此,现有的生成线性含十氟联苯的聚合物,通常都是采用溶液浇铸法制备成膜材料应用,如中国专利CN111530511A、CN111662446A、CN111363140A和CN110756060A。然而,溶液浇铸法只能制备膜材料,难以加工成管材、棒材和板材等体型材料,这在一定程度上限制了含氟聚合物在其他领域的应用。For traditional thermoplastic resins, melt processing is one of the important means of shaping and processing body materials. However, the polymer prepared by using decafluorobiphenyl monomer has reactive activity because all ten fluorine atoms of the monomer are reactive, so it is very easy to react with the active end groups remaining in the polymerization reaction during the polymerization reaction and high temperature processing, resulting in branching, Structures such as crosslinking affect the fluidity and stability of the melt, and are not conducive to melt processing to construct bulk materials. Therefore, the existing linear decafluorobiphenyl-containing polymers are usually prepared by solution casting for application as film-forming materials, such as Chinese patents CN111530511A, CN111662446A, CN111363140A and CN110756060A. However, the solution casting method can only prepare membrane materials, and it is difficult to process them into bulk materials such as pipes, rods and sheets, which limits the application of fluoropolymers in other fields to a certain extent.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种可熔融加工封端含氟聚芳醚树脂及其制备方法和应用,所制备的封端含氟聚芳醚树脂可熔融加工,扩展了含氟聚芳醚树脂的应用范围。The object of the present invention is to provide a melt-processable end-capped fluorine-containing polyarylether resin and a preparation method and application thereof. Scope of application.
为了实现上述发明目的,本发明提供以下技术方案:In order to achieve the above-mentioned purpose of the invention, the present invention provides the following technical solutions:
本发明提供了一种封端含氟聚芳醚树脂的制备方法,包括以下步骤:The invention provides a preparation method of end-capped fluorine-containing polyarylene ether resin, comprising the following steps:
将双酚单体、成盐剂、脱水剂和非质子极性有机溶剂混合,进行成盐反应,得到第一产物;Mixing the bisphenol monomer, the salt-forming agent, the dehydrating agent and the aprotic polar organic solvent to carry out a salt-forming reaction to obtain the first product;
将所述第一产物与十氟联苯混合,进行聚合反应,向所得产物中加入封端剂,进行封端,得到封端含氟聚芳醚树脂;Mixing the first product with decafluorobiphenyl, carrying out a polymerization reaction, adding an end-capping agent to the obtained product, and capping to obtain an end-capped fluorine-containing polyarylene ether resin;
所述封端剂包括4,4’-二氟二苯砜、4,4’二氟二苯甲酮、3,3’二氟二苯甲酮、4-氟苯基苯砜或4-氟二苯甲酮。The capping agent includes 4,4'-difluorodiphenylsulfone, 4,4'difluorobenzophenone, 3,3'difluorobenzophenone, 4-fluorophenylphenylsulfone, or 4-fluoro Benzophenone.
优选的,所述双酚单体包括双酚A、双酚AF和双酚芴中的一种或几种。Preferably, the bisphenol monomer includes one or more of bisphenol A, bisphenol AF and bisphenol fluorene.
优选的,所述十氟联苯与所述双酚单体的摩尔比为(0.95~1.05):1。Preferably, the molar ratio of the decafluorobiphenyl to the bisphenol monomer is (0.95-1.05):1.
优选的,所述成盐剂包括碳酸铯、碳酸钾和碳酸钠中的一种或几种;所述成盐剂与所述双酚单体的摩尔比为(1.001~1.35):1。Preferably, the salt-forming agent comprises one or more of cesium carbonate, potassium carbonate and sodium carbonate; the molar ratio of the salt-forming agent to the bisphenol monomer is (1.001-1.35):1.
优选的,所述脱水剂包括甲苯、二甲苯和环己烷中的一种或几种;所述非质子极性有机溶剂包括二甲基甲酰胺、二甲基乙酰胺、环丁砜或N-甲基吡咯烷酮;所述脱水剂的体积为所述非质子极性有机溶剂体积的30~50%。Preferably, the dehydrating agent includes one or more of toluene, xylene and cyclohexane; the aprotic polar organic solvent includes dimethylformamide, dimethylacetamide, sulfolane or N-methylformamide pyrrolidone; the volume of the dehydrating agent is 30-50% of the volume of the aprotic polar organic solvent.
优选的,所述双酚单体和十氟联苯在非质子极性有机溶剂中的总固含量为10~25wt%。Preferably, the total solid content of the bisphenol monomer and decafluorobiphenyl in the aprotic polar organic solvent is 10-25 wt%.
优选的,所述封端剂与所述双酚单体的摩尔比为(0.01~0.05):1。Preferably, the molar ratio of the capping agent to the bisphenol monomer is (0.01-0.05):1.
本发明提供了上述技术方案所述制备方法制备得到的封端含氟聚芳醚树脂,具有式I所示结构:The present invention provides the end-capped fluorine-containing polyarylether resin prepared by the preparation method described in the above technical solution, which has the structure shown in formula I:
式I中,n为聚合度,n=2×104~1×105;R为双酚单体去除两端酚羟基所对应的基团,R1包括In formula I, n is the degree of polymerization, n=2×10 4 to 1×10 5 ; R is the group corresponding to the removal of the phenolic hydroxyl groups at both ends of the bisphenol monomer, and R 1 includes
优选的,包括preferably, including
n=6×104、 n=6×10 4 ,
n=7×104或 n=7× 104 or
n=8×104。 n=8×10 4 .
本发明提供了上述技术方案所述封端含氟聚芳醚树脂在制备热稳定性体型材料中的应用。The present invention provides the application of the end-capped fluorine-containing polyarylene ether resin in the preparation of a thermally stable bulk material according to the above technical solution.
本发明提供了一种封端含氟聚芳醚树脂的制备方法,包括以下步骤:将双酚单体、成盐剂、脱水剂和非质子极性有机溶剂混合,进行成盐反应,得到第一产物;将所述第一产物与十氟联苯混合,进行聚合反应,向所得产物中加入封端剂,进行封端,得到封端含氟聚芳醚树脂;所述封端剂包括十氟联苯、4,4’-二氟二苯砜、4,4’二氟二苯甲酮、3,3’二氟二苯甲酮、4-氟苯基苯砜或4-氟二苯甲酮。本发明采用含有单氟基团的稳定芳香单体作为封端剂,利用封端剂含有两个或单个氟基团的结构,充分消除聚合物末端双酚单体未反应的活性的酚羟基端基,降低十氟联苯在高温熔融加工过程中侧位氟基团与活性端基发生支化交联的情况,改善熔融加工过程中因产生支化交联结构而影响熔体流动性和稳定性的问题,实现含氟聚芳醚聚合物的熔融加工,为获得具有高热稳定性的体型材料提供了新思路。The present invention provides a method for preparing an end-capped fluorine-containing polyarylene ether resin. a product; the first product is mixed with decafluorobiphenyl to carry out a polymerization reaction, and an end-capping agent is added to the obtained product to perform end-capping to obtain an end-capped fluorine-containing polyarylene ether resin; the end-capping agent includes ten Fluorobiphenyl, 4,4'-difluorodiphenylsulfone, 4,4'difluorobenzophenone, 3,3'difluorobenzophenone, 4-fluorophenylphenylsulfone, or 4-fluorodiphenyl ketone. The invention adopts a stable aromatic monomer containing a single fluorine group as the end-capping agent, and utilizes the structure of the end-capping agent containing two or single fluorine groups to fully eliminate the unreacted active phenolic hydroxyl end of the bisphenol monomer at the polymer end It can reduce the branching and cross-linking of the lateral fluorine group and the active end group of decafluorobiphenyl during high-temperature melt processing, and improve the melt fluidity and stability of the melt due to the branched cross-linking structure during melt processing. To solve the problem of properties, realize the melt processing of fluorine-containing polyarylene ether polymers, which provides a new idea for obtaining bulk materials with high thermal stability.
本发明所用封端剂具有与双酚单体相似的官能团结构,且氟基团反应活性较大,既可以避免在聚合物引入其他基团对聚合物性能产生较大影响,同时保证聚合物的线性结构不被改变,从而保证熔体具有一定的流动性,有利于挤出熔融加工。The end-capping agent used in the present invention has a similar functional group structure as the bisphenol monomer, and the fluorine group has high reactivity, which can not only avoid the introduction of other groups into the polymer to have a great influence on the performance of the polymer, but also ensure the polymer's performance. The linear structure is not changed, so as to ensure that the melt has a certain fluidity, which is beneficial to extrusion melt processing.
本发明在聚合反应后期进行封端处理的方法获得高含氟量的含氟聚芳醚树脂线性材料,并能够通过改变双酚单体与十氟联苯的投料比例降低聚合物分子量大小来提高熔体流动性,制得可用于熔融加工的含氟聚芳醚树脂,本发明的方法封端效果好,封端后的树脂产品可通过熔融加工方法获得体型材料的封端聚芳醚树脂。The method of carrying out end-capping treatment in the later stage of the polymerization reaction of the present invention obtains a linear material of fluorine-containing polyarylene ether resin with high fluorine content, and can reduce the molecular weight of the polymer by changing the feeding ratio of bisphenol monomer and decafluorobiphenyl to improve the The melt fluidity is improved, and the fluorine-containing polyarylene ether resin that can be used for melt processing is prepared. The method of the present invention has a good end-capping effect, and the end-capped resin product can obtain the end-capped polyarylene ether resin of the body shape material by the melt processing method.
本发明的方法打破了传统含氟聚合物只能通过溶液浇铸法获得膜材料的局限性,不仅可以节省溶液浇铸法中溶剂的使用,减少有机溶剂对环境的污染和危害,还可以获得不同形状的体型材料应用在各个领域,充分发挥氟材料在减磨耐磨方面的优势。The method of the invention breaks the limitation that the traditional fluorine-containing polymer can only obtain the membrane material through the solution casting method, not only can save the use of the solvent in the solution casting method, reduce the pollution and harm of the organic solvent to the environment, but also can obtain different shapes The body type materials are used in various fields, giving full play to the advantages of fluorine materials in wear reduction and wear resistance.
附图说明Description of drawings
图1为实施例1制备的封端含氟聚芳醚的核磁H1图;Fig. 1 is the nuclear magnetic H 1 diagram of the end-capped fluorine-containing polyarylene ether prepared in Example 1;
图2为实施例1制备的封端含氟聚芳醚的核磁F19图;Fig. 2 is the NMR F 19 diagram of the end-capped fluorine-containing polyarylene ether prepared in Example 1;
图3为实施例3制备的封端含氟聚芳醚的核磁H1图;Fig. 3 is the nuclear magnetic H 1 map of the end-capped fluorine-containing polyarylene ether prepared in Example 3;
图4为实施例3制备的封端含氟聚芳醚的核磁F19图;Fig. 4 is the nuclear magnetic F 19 image of the end-capped fluorine-containing polyarylene ether prepared in Example 3;
图5为实施例1制备的封端含氟聚芳醚的熔融挤出样条图;Fig. 5 is the melt extrusion spline diagram of the end-capped fluorine-containing polyarylene ether prepared in Example 1;
图6为实施例1制备的封端含氟聚芳醚的可供机械性能、摩擦性能测试所需的样条实物图;Fig. 6 is the physical drawing of the spline required for the mechanical property and friction property test of the end-capped fluorine-containing polyarylene ether prepared in Example 1;
具体实施方式Detailed ways
本发明提供了一种封端含氟聚芳醚树脂的制备方法,包括以下步骤:The invention provides a preparation method of end-capped fluorine-containing polyarylene ether resin, comprising the following steps:
将双酚单体、成盐剂、脱水剂和非质子极性有机溶剂混合,进行成盐反应,得到第一产物;Mixing the bisphenol monomer, the salt-forming agent, the dehydrating agent and the aprotic polar organic solvent to carry out a salt-forming reaction to obtain the first product;
将所述第一产物与十氟联苯混合,进行聚合反应,向所得产物中加入封端剂,进行封端,得到封端含氟聚芳醚树脂;Mixing the first product with decafluorobiphenyl, carrying out a polymerization reaction, adding an end-capping agent to the obtained product, and capping to obtain an end-capped fluorine-containing polyarylene ether resin;
所述封端剂包括4,4’-二氟二苯砜、4,4’二氟二苯甲酮、3,3’二氟二苯甲酮、4-氟苯基苯砜或4-氟二苯甲酮。The capping agent includes 4,4'-difluorodiphenylsulfone, 4,4'difluorobenzophenone, 3,3'difluorobenzophenone, 4-fluorophenylphenylsulfone, or 4-fluoro Benzophenone.
在本发明中,若无特殊说明,所需制备原料均为本领域技术人员熟知的市售商品。In the present invention, unless otherwise specified, the required preparation raw materials are all commercially available products well known to those skilled in the art.
本发明将双酚单体、成盐剂、脱水剂和非质子极性有机溶剂混合,进行成盐反应,得到第一产物。在本发明中,所述双酚单体优选包括双酚A、双酚AF和双酚芴中的一种或几种;当所述双酚单体为上述中的几种时,本发明对不同种类双酚单体的配比没有特殊的限定,任意配比均可。In the present invention, the bisphenol monomer, the salt-forming agent, the dehydrating agent and the aprotic polar organic solvent are mixed, and the salt-forming reaction is carried out to obtain the first product. In the present invention, the bisphenol monomer preferably includes one or more of bisphenol A, bisphenol AF and bisphenol fluorene; when the bisphenol monomer is several of the above, the The ratio of different types of bisphenol monomers is not particularly limited, and any ratio can be used.
在本发明中,所述成盐剂优选包括碳酸铯、碳酸钾和碳酸钠中的一种或几种;当所述成盐剂为上述中的几种时,本发明对不同种类成盐剂的配比没有特殊的限定,任意配比均可。在本发明中,所述成盐剂与所述双酚单体的摩尔比优选为(1.001~1.35):1,更优选为(1.1~1.25):1。In the present invention, the salt-forming agent preferably includes one or more of cesium carbonate, potassium carbonate and sodium carbonate; when the salt-forming agent is several of the above, the present invention is suitable for different types of salt-forming agents. There is no special restriction on the ratio of , and any ratio can be used. In the present invention, the molar ratio of the salt-forming agent to the bisphenol monomer is preferably (1.001-1.35):1, more preferably (1.1-1.25):1.
在本发明中,所述脱水剂优选包括甲苯、二甲苯和环己烷中的一种或几种;当所述成盐剂为上述中的几种时,本发明对不同种类成盐剂的配比没有特殊的限定,任意配比均可。In the present invention, the dehydrating agent preferably includes one or more of toluene, xylene and cyclohexane; when the salt-forming agent is several of the above, the There is no special restriction on the ratio, and any ratio can be used.
在本发明中,所述非质子极性有机溶剂优选包括二甲基甲酰胺、二甲基乙酰胺、环丁砜或N-甲基吡咯烷酮;所述脱水剂的体积优选为所述非质子极性有机溶剂体积的30~50%,更优选为35~45%。In the present invention, the aprotic polar organic solvent preferably includes dimethylformamide, dimethylacetamide, sulfolane or N-methylpyrrolidone; the volume of the dehydrating agent is preferably the same as that of the aprotic polar organic solvent 30 to 50% of the solvent volume, more preferably 35 to 45%.
在本发明中,所述双酚单体、成盐剂、脱水剂和非质子极性有机溶剂混合的过程优选在搅拌条件下进行,所述搅拌的时间优选为0.5~1h。本发明对所述搅拌的速率没有特殊的限定,按照本领域熟知的速率搅拌即可。In the present invention, the process of mixing the bisphenol monomer, the salt-forming agent, the dehydrating agent and the aprotic polar organic solvent is preferably performed under stirring conditions, and the stirring time is preferably 0.5-1 h. The present invention does not have a special limitation on the stirring speed, and the stirring speed is well known in the art.
在本发明中,所述成盐反应优选在氩气气氛下进行;所述成盐反应的温度优选为110~140℃,更优选为120~130℃;时间优选为2~4h,更优选为2.5~3.5h。本发明对升温至所述成盐反应的温度的升温速率没有特殊的限定,按照本领域熟知的速率升温即可。在所述成盐反应过程中,双酚单体和成盐剂成盐产生的水与脱水剂进行共沸脱水,脱水剂通过分水器除去;完成所述成盐反应后,本发明优选升温至脱水剂沸点以上,排出脱水剂。In the present invention, the salt-forming reaction is preferably carried out in an argon atmosphere; the temperature of the salt-forming reaction is preferably 110-140°C, more preferably 120-130°C; the time is preferably 2-4h, more preferably 2.5~3.5h. The present invention has no particular limitation on the rate of temperature increase to the temperature of the salt-forming reaction, and the temperature may be increased according to a rate well known in the art. During the salt-forming reaction, the water produced by the salt-forming of the bisphenol monomer and the salt-forming agent is subjected to azeotropic dehydration with the dehydrating agent, and the dehydrating agent is removed by a water separator; after the salt-forming reaction is completed, the present invention preferably raises the temperature To above the boiling point of the dehydrating agent, discharge the dehydrating agent.
排出脱水剂后,本发明优选将所得反应料液冷却至室温,得到第一产物。After discharging the dehydrating agent, the present invention preferably cools the obtained reaction feed liquid to room temperature to obtain the first product.
得到第一产物后,本发明将所述第一产物与十氟联苯混合,进行聚合反应,向所得产物中加入封端剂,进行封端,得到封端含氟聚芳醚树脂。在本发明中,所述十氟联苯与所述双酚单体的摩尔比优选为(0.95~1.05):1,更优选为(1.02~1.03):1。在本发明中,所述双酚单体和十氟联苯在非质子极性有机溶剂中的总固含量优选为10~25wt%,更优选为15~20wt%。After the first product is obtained, in the present invention, the first product is mixed with decafluorobiphenyl to carry out a polymerization reaction, and an end capping agent is added to the obtained product to perform end capping to obtain an end capped fluorine-containing polyarylene ether resin. In the present invention, the molar ratio of the decafluorobiphenyl to the bisphenol monomer is preferably (0.95-1.05):1, more preferably (1.02-1.03):1. In the present invention, the total solid content of the bisphenol monomer and decafluorobiphenyl in the aprotic polar organic solvent is preferably 10-25 wt %, more preferably 15-20 wt %.
在本发明中,所述封端剂包括4,4’-二氟二苯砜、4,4’二氟二苯甲酮、3,3’二氟二苯甲酮、4-氟苯基苯砜或4-氟二苯甲酮;优选为4,4’-二氟二苯砜、4-氟苯基苯砜或4-氟二苯甲酮。In the present invention, the end-capping agent includes 4,4'-difluorodiphenylsulfone, 4,4'difluorobenzophenone, 3,3'difluorobenzophenone, 4-fluorophenylbenzene Sulfone or 4-fluorobenzophenone; preferably 4,4'-difluorodiphenylsulfone, 4-fluorophenylphenylsulfone or 4-fluorobenzophenone.
在本发明中,所述封端剂的结构式具体为:In the present invention, the structural formula of the end-capping agent is specifically:
(4,4’-二氟二苯砜)、(4,4’二氟二苯甲酮)、(3,3’二氟二苯甲酮)、(4-氟苯基苯砜)或(4-氟二苯甲酮)。 (4,4'-difluorodiphenylsulfone), (4,4'difluorobenzophenone), (3,3'difluorobenzophenone), (4-Fluorophenylphenylsulfone) or (4-Fluorobenzophenone).
在本发明中,所述封端剂与所述双酚单体的摩尔比优选为(0.01~0.05):1,更优选为(0.02~0.03):1。In the present invention, the molar ratio of the capping agent to the bisphenol monomer is preferably (0.01-0.05):1, more preferably (0.02-0.03):1.
本发明优选向所述第一产物中加入十氟联苯,搅拌混合均匀。本发明对所述搅拌的过程没有特殊的限定,按照本领域熟知的过程进行即可。In the present invention, decafluorobiphenyl is preferably added to the first product, and the mixture is stirred and mixed evenly. The present invention does not have a special limitation on the stirring process, and it can be carried out according to a well-known process in the art.
在本发明中,所述聚合反应优选在氩气气氛下进行。In the present invention, the polymerization reaction is preferably carried out under an argon atmosphere.
在本发明中,所述聚合反应的过程优选包括:第一升温至30~40℃,进行第一聚合反应6~12h,第二升温至50~70℃,进行第二聚合反应6~12h,第三升温至80~100℃,进行第三聚合反应6~12h。本发明对所述第一升温、第二升温和第三升温的升温速率没有特殊的限定,按照本领域熟知的速率升温即可。In the present invention, the process of the polymerization reaction preferably includes: firstly raising the temperature to 30-40°C, performing the first polymerization reaction for 6-12 hours, and secondly raising the temperature to 50-70°C, performing the second polymerization reaction for 6-12 hours, The third temperature is raised to 80-100° C., and the third polymerization reaction is carried out for 6-12 hours. The present invention does not specifically limit the heating rates of the first, second, and third temperature rises, and the temperature rises at rates well known in the art.
完成所述聚合反应后,本发明向所得物料中加入封端剂,在80~100℃进行第一封端1~2h,然后梯度升温至120~130℃,进行第二封端1~2h,然后梯度升温至140~160℃,进行第三封端1~2h。本发明对所述梯度升温的升温速率没有特殊的限定,按照本领域熟知的梯度速率升温即可。After the polymerization reaction is completed, the present invention adds an end-capping agent to the obtained material, performs the first end-capping at 80-100° C. for 1-2 hours, and then ramps the temperature to 120-130° C. and performs the second end-capping for 1-2 hours. Then, the temperature is gradually increased to 140-160° C., and the third end capping is performed for 1-2 h. The present invention does not have a special limitation on the heating rate of the gradient heating, and the temperature may be increased according to the gradient rate well known in the art.
完成所述封端后,本发明优选将所得聚合物粘液置于去离子水中析出,将所得析出物依次进行粉碎、过滤、洗涤和干燥,得到封端含氟聚芳醚树脂。在本发明中,所述洗涤优选依次采用低沸点有机溶剂和去离子水煮沸洗涤;所述低沸点有极溶剂优选为甲醇和/或乙醇;当所述低沸点有机溶剂为甲醇和乙醇时,本发明对甲醇和乙醇的配比没有特殊的限定,任意配比均可。After the end capping is completed, in the present invention, the obtained polymer mucus is preferably placed in deionized water for precipitation, and the obtained precipitation is sequentially pulverized, filtered, washed and dried to obtain an end capped fluorine-containing polyarylene ether resin. In the present invention, the washing preferably adopts a low-boiling organic solvent and deionized water to boil and wash in sequence; the low-boiling polar solvent is preferably methanol and/or ethanol; when the low-boiling organic solvent is methanol and ethanol, The present invention has no special limitation on the ratio of methanol and ethanol, and any ratio can be used.
本发明对所述洗涤的次数没有特殊的限定,能够完全除去溶剂和副产物盐即可;本发明对所述粉碎、过滤和干燥的过程没有特殊的限定,按照本领域熟知的过程进行即可。The present invention has no special limitation on the number of times of washing, as long as the solvent and by-product salt can be completely removed; the present invention has no special limitation on the processes of pulverization, filtration and drying, and can be carried out according to well-known processes in the art. .
本发明提供了上述技术方案所述制备方法制备得到的封端含氟聚芳醚树脂,具有式I所示结构:The present invention provides the end-capped fluorine-containing polyarylether resin prepared by the preparation method described in the above technical solution, which has the structure shown in formula I:
式I中,n为聚合度,n=2×104~1×105;R为双酚单体去除两端酚羟基所对应的基团,R1包括In formula I, n is the degree of polymerization, n=2×10 4 to 1×10 5 ; R is the group corresponding to the removal of the phenolic hydroxyl groups at both ends of the bisphenol monomer, and R 1 includes
优选的,包括preferably, including
n=6×104、 n=6×10 4 ,
n=7×104或 n=7× 104 or
n=8×104。 n=8×10 4 .
本发明提供了上述技术方案所述封端含氟聚芳醚树脂在制备热稳定性体型材料中的应用。本发明对所述应用的方法没有特殊的限定,按照本领域熟知的方法将所述封端含氟聚芳醚树脂制成体型材料即可。The present invention provides the application of the end-capped fluorine-containing polyarylene ether resin in the preparation of a thermally stable bulk material according to the above technical solution. The application method is not particularly limited in the present invention, and the end-capped fluorine-containing polyarylene ether resin can be made into a body-shaped material according to a method well known in the art.
下面将结合本发明中的实施例,对本发明中的技术方案进行清楚、完整地描述。显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only some, but not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
将420mLN,N-二甲基乙酰胺、200mL甲苯、0.1mol双酚AF和0.12mol无水碳酸钾装入1000mL三口烧瓶中,在氩气气氛下,机械搅拌1h后,升温至135℃,共沸脱水回流2.5h,升温至152℃,排出脱水剂,将反应体系温度降至室温后,将0.104mol十氟联苯加入反应体系中,双酚AF和十氟联苯的总固含量为15wt%,搅拌均匀后升温至40℃,反应12h,升温到60℃,反应12h,升温80℃,反应12h,然后向所得物料中加入0.002mol 4,4’-二氟二苯砜,在80℃反应2h,升温至120℃,反应2h,升温至160℃,反应2h,将所得聚合物粘液在去离子水中析出,将所得析出物粉碎后,依次采用甲醇和去离子水煮沸洗涤,干燥后,得到封端含氟聚芳醚树脂,结构式为:420 mL of N,N-dimethylacetamide, 200 mL of toluene, 0.1 mol of bisphenol AF and 0.12 mol of anhydrous potassium carbonate were placed in a 1000 mL three-necked flask. Boiling dehydration and refluxing for 2.5h, the temperature was raised to 152°C, the dehydrating agent was discharged, and after the temperature of the reaction system was lowered to room temperature, 0.104mol decafluorobiphenyl was added to the reaction system, and the total solid content of bisphenol AF and decafluorobiphenyl was 15wt %, stir evenly, then heat up to 40°C, react for 12h, heat up to 60°C, react for 12h, heat up to 80°C, react for 12h, then add 0.002mol 4,4'-difluorodiphenylsulfone to the obtained material, at 80°C React for 2 hours, heat up to 120 °C, react for 2 hours, heat up to 160 °C, react for 2 hours, and separate the obtained polymer mucilage in deionized water. The end-capped fluorine-containing polyarylene ether resin is obtained, and the structural formula is:
n=6×104。 n=6×10 4 .
对实施例1制备的封端含氟聚芳醚树脂进行熔融指数、比浓粘度和玻璃化转变温度测试,其中熔融指数测试标准为260℃,压力5Kg;比浓粘度测试中聚合物的浓度为0.5g/dL;DSC测试温度范围80~400℃,在N2气氛下进行;结果表明:封端含氟聚芳醚酮树脂熔融指数MI=7.0g/10min(260.0℃,5KG,5分钟);MI=6.6g/10min(260.0℃,5KG,30分钟);在NMP中的比浓粘度ηsp/c=0.25[dL/g](25℃);Tg:174℃。The melt index, reduced viscosity and glass transition temperature of the end-capped fluorine-containing polyarylene ether resin prepared in Example 1 were tested, wherein the melt index test standard was 260° C. and the pressure was 5Kg; the concentration of the polymer in the reduced viscosity test was 0.5g/dL; DSC test temperature range is 80~400℃, under N 2 atmosphere; the results show that: end-capped fluorine-containing polyaryletherketone resin melt index MI=7.0g/10min (260.0℃, 5KG, 5 minutes) ; MI=6.6 g/10min (260.0°C, 5KG, 30 minutes); Reduced viscosity in NMP η sp /c=0.25 [dL/g] (25°C); Tg: 174°C.
实施例2Example 2
将500mL二甲基乙酰胺、250mL甲苯、0.12mol双酚AF和0.144mol无水碳酸钾装入1000mL三口烧瓶中,在氩气气氛下,机械搅拌1h后,升温至132℃,共沸脱水回流2.5h,升温至147℃,排出脱水剂,将反应体系温度降至室温后,将0.1236mol十氟联苯加入反应体系中,双酚AF和十氟联苯的总固含量为15wt%,搅拌均匀后升温至40℃,反应12h,升温到60℃,反应12h,升温80℃,反应12h,然后向所得物料中加入0.006mol 4-氟二苯甲酮,在80℃反应2h,升温到120℃,反应2h,升温到160℃,反应2h,将所得聚合物粘液在去离子水中析出,将所得析出物粉碎后,依次采用甲醇和去离子水煮沸洗涤,干燥后,得到封端含氟聚芳醚树脂,结构式为:500 mL of dimethylacetamide, 250 mL of toluene, 0.12 mol of bisphenol AF and 0.144 mol of anhydrous potassium carbonate were placed in a 1000 mL three-necked flask, under argon atmosphere, mechanically stirred for 1 h, then heated to 132 ° C, azeotropic dehydration and reflux After 2.5h, the temperature was raised to 147°C, the dehydrating agent was discharged, and the temperature of the reaction system was lowered to room temperature, and 0.1236mol of decafluorobiphenyl was added to the reaction system. After uniform, the temperature was raised to 40°C, reacted for 12h, heated to 60°C, reacted for 12h, heated to 80°C, reacted for 12h, then added 0.006mol 4-fluorobenzophenone to the obtained material, reacted at 80°C for 2h, and heated to 120°C ℃, reacted for 2h, heated to 160℃, reacted for 2h, precipitated the obtained polymer mucilage in deionized water, pulverized the obtained precipitate, boiled and washed with methanol and deionized water in turn, and dried to obtain the end-capped fluoropolymer. Aromatic ether resin, the structural formula is:
n=7×104。 n=7×10 4 .
按照实施例1所述方法,对实施例2制备的封端含氟聚芳醚酮树脂进行测试,结果表明:封端含氟聚芳醚酮树脂的熔融指数MI=6.4g/10min(280.0℃,5KG,5分钟);MI=6.0g/10min(280.0℃,5KG,30分钟);在NMP中的比浓粘度ηsp/c=0.28[dL/g](25℃);Tg:188℃。According to the method described in Example 1, the end-capped fluorine-containing polyaryl ether ketone resin prepared in Example 2 was tested. , 5KG, 5 minutes); MI=6.0g/10min (280.0°C, 5KG, 30 minutes); Reduced viscosity in NMP η sp /c=0.28 [dL/g] (25°C); Tg: 188°C .
实施例3Example 3
将120mL二甲基乙酰胺、50mL甲苯、0.05mol双酚A和0.06mol无水碳酸钾装入250mL三口烧瓶中,在氩气气氛下,机械搅拌0.5h后,升温至130℃,共沸脱水回流2h,升温至146℃,排出脱水剂,将反应体系温度降至室温后,将0.051mol十氟联苯加入反应体系中,双酚A和十氟联苯的总的固含量为20wt%,搅拌均匀后升温至40℃,反应12h,升温到60℃,反应12h,升温80℃,反应12h,然后向所得物料中加入0.0025mol 4,4’二氟二苯甲酮,在80℃反应2h,升温到120℃,反应2h,升温到160℃,反应2h,将所得聚合物粘液在去离子水中析出,将所得析出物粉碎后,依次采用甲醇和去离子水煮沸洗涤,干燥后,得到封端含氟聚芳醚树脂,结构式为:Put 120 mL of dimethylacetamide, 50 mL of toluene, 0.05 mol of bisphenol A and 0.06 mol of anhydrous potassium carbonate into a 250 mL three-necked flask, and under argon atmosphere, mechanically stir for 0.5 h, then heat up to 130 °C, and azeotropically dehydrate Reflux for 2h, heat up to 146°C, discharge the dehydrating agent, and after the temperature of the reaction system is lowered to room temperature, 0.051mol of decafluorobiphenyl is added to the reaction system, and the total solid content of bisphenol A and decafluorobiphenyl is 20wt%, After stirring evenly, the temperature was raised to 40°C, reacted for 12h, heated to 60°C, reacted for 12h, heated to 80°C, reacted for 12h, then added 0.0025mol 4,4'difluorobenzophenone to the obtained material, and reacted at 80°C for 2h , heated to 120 °C, reacted for 2 h, heated to 160 °C, reacted for 2 h, the obtained polymer mucus was precipitated in deionized water, the obtained precipitate was pulverized, boiled and washed with methanol and deionized water in turn, and dried to obtain a sealant. Terminal fluorine-containing polyarylene ether resin, the structural formula is:
n=8×104。 n=8×10 4 .
按照实施例1所述方法,对实施例3制备的封端含氟聚芳醚酮树脂进行测试,结果表明:封端含氟聚芳醚酮树脂的熔融指数MI=10.0g/10min(280.0℃,5KG,5分钟);MI=8.9g/10min(280.0℃,5KG,30分钟);在NMP中的比浓粘度ηsp/c=0.38[dL/g](25℃);Tg:168℃。According to the method described in Example 1, the end-capped fluorine-containing polyaryletherketone resin prepared in Example 3 was tested. , 5KG, 5 minutes); MI=8.9g/10min (280.0°C, 5KG, 30 minutes); Reduced viscosity in NMP η sp /c=0.38 [dL/g] (25°C); Tg: 168°C .
对比例1Comparative Example 1
将410mL二甲基乙酰胺、150mL甲苯、0.1mol双酚AF和0.12mol无水碳酸钾装入1000mL三口烧瓶中,在氩气气氛下,机械搅拌1h后,升温至130℃,共沸脱水回流1.5h,升温至138℃,排出脱水剂,将反应体系温度降至室温后,将0.102mol十氟联苯加入反应体系中,双酚AF和十氟联苯的总固含量为15wt%,搅拌均匀后升温至80℃,反应24h,将所得聚合物粘液在去离子水中析出,将所得析出物粉碎后,依次采用甲醇和去离子水煮沸洗涤,干燥后,得到未封端的含氟聚芳醚酮树脂,结构式为Put 410 mL of dimethylacetamide, 150 mL of toluene, 0.1 mol of bisphenol AF and 0.12 mol of anhydrous potassium carbonate into a 1000 mL three-necked flask, under argon atmosphere, mechanically stir for 1 h, then heat up to 130 ° C, azeotropic dehydration and reflux After 1.5h, the temperature was raised to 138°C, the dehydrating agent was discharged, and the temperature of the reaction system was lowered to room temperature. After uniform, the temperature was raised to 80°C, and the reaction was carried out for 24 hours. The obtained polymer mucilage was precipitated in deionized water. The obtained precipitate was pulverized, boiled and washed with methanol and deionized water in turn, and dried to obtain uncapped fluorine-containing polyarylene ether. Ketone resin, the structural formula is
n≈8×104。 n≈8×10 4 .
按照实施例1所述方法,对对比例1制备的含氟聚芳醚酮树脂进行测试,结果表明:对比例1制备的含氟聚芳醚酮树脂无法进行熔融指数测定;在NMP中的比浓粘度ηsp/c=0.36[dL/g](25℃);Tg:185℃。According to the method described in Example 1, the fluorinated polyaryletherketone resin prepared in Comparative Example 1 was tested, and the results showed that: the fluorinated polyaryletherketone resin prepared in Comparative Example 1 could not be measured for melt index; Thick viscosity η sp /c = 0.36 [dL/g] (25°C); Tg: 185°C.
表征及性能测试Characterization and Performance Testing
1)对实施例1制备的封端含氟聚芳醚树脂进行核磁表征,所得结果见图1~2;由图1~2可知,在1H-NMR谱图1中可以看到在7.91ppm和7.19ppm的两组吸收来自于苯环上的两类氢原子“1”和“2”,在19F-NMR谱图2中,“1”属于双酚AF中的六氟异丙基,“2”和“3”分别属于十氟联苯上邻位和间位氟原子,通过核磁谱图证实本发明成功制得线性的封端含氟聚合物。实施例2制备的封端含氟聚芳醚树脂与实施例1具有相同的核磁谱图。1) Carry out NMR characterization on the end-capped fluorine-containing polyarylether resin prepared in Example 1, and the obtained results are shown in Figures 1-2; it can be seen from Figures 1-2 that the 1 H-NMR spectrum in Figure 1 can be seen at 7.91 ppm and 7.19ppm of two groups of absorptions come from two types of hydrogen atoms "1" and "2" on the benzene ring, in the 19 F-
2)对实施例3制备的含氟聚芳醚树脂进行核磁表征,所得结果见图3~4;在1H-NMR谱图3中可以看到,在6.97ppm和7.23ppm的两组吸收来自苯环上的两类氢原子“1”和“2”,在1.70ppm处的吸收峰来自异丙基上的氢原子,在19F-NMR谱图4中可以看到,“1”和“2”分别属于十氟联苯上邻位和间位氟原子,通过核磁谱图证明实例3成功合成线性的封端含氟聚合物。2) Carry out nuclear magnetic characterization on the fluorine-containing polyarylene ether resin prepared in Example 3, and the obtained results are shown in Figures 3-4; it can be seen in Figure 3 of the 1 H-NMR spectrum that the two groups of absorptions at 6.97 ppm and 7.23 ppm come from Two types of hydrogen atoms "1" and "2" on the benzene ring, the absorption peak at 1.70ppm is from the hydrogen atom on the isopropyl group, it can be seen in the 19 F-NMR spectrum Figure 4, "1" and " 2” belong to the ortho and meta fluorine atoms on decafluorobiphenyl, respectively. It is proved by the nuclear magnetic spectrum that the linear end-capped fluorine-containing polymer is successfully synthesized in Example 3.
3)图5为在260℃下对实施例1所制备的封端含氟聚芳醚进行熔融注射加工的熔融挤出样条实物图;图6为采用熔融挤出将实施例1制备的封端含氟聚芳醚制成的供机械性能、摩擦性能测试所需的样条实物图;由图5和图6可知,熔融挤出样条表面光滑,颜色为淡黄色,可以证明其熔体具有良好的流动性和稳定性,且能得到完整的供测试所用的样条,证明其可以进行熔融加工。3) Fig. 5 is a real picture of a melt-extruded spline for melt-injection processing of the capped fluorinated polyarylene ether prepared in Example 1 at 260°C; Figure 5 and Figure 6 show that the surface of the melt extruded spline is smooth and the color is light yellow, which can prove that its melt It has good flow and stability, and can get a complete test strip, which proves that it can be melt processed.
6)对实施例1~3制备的封端含氟聚芳醚树脂进行力学性能、摩擦性能和表面能测试,其中,机械性能采用GB/T 9341-2008标准进行测试;摩擦性能采用环-块式摩擦磨损试验机进行测试,对偶面为45#钢环,压力为30N,转速为200rpm,滑动时间为2h;所得结果见表1。6) The mechanical properties, friction properties and surface energy of the end-capped fluorinated polyarylene ether resins prepared in Examples 1-3 were tested, wherein the mechanical properties were tested by the GB/T 9341-2008 standard; the friction properties were tested by ring-block Type friction and wear testing machine was used to test, the dual surface was 45# steel ring, the pressure was 30N, the speed was 200rpm, and the sliding time was 2h; the results obtained are shown in Table 1.
表1实施例1~3制备的封端含氟聚芳醚树脂进行力学性能、摩擦性能和表面能数据Table 1 Mechanical properties, friction properties and surface energy data of the end-capped fluorine-containing polyarylene ether resins prepared in Examples 1-3
对比实施例1~3发现,实施例1和实施例2所制备的封端含氟聚合物分子量略高,所以各项性能也略微提高。Comparing Examples 1 to 3, it is found that the molecular weights of the end-capped fluoropolymers prepared in Examples 1 and 2 are slightly higher, so various properties are also slightly improved.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the principles of the present invention, several improvements and modifications can be made. It should be regarded as the protection scope of the present invention.
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