WO2010099645A1 - Method for coupling polyolefin chains - Google Patents
Method for coupling polyolefin chains Download PDFInfo
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- WO2010099645A1 WO2010099645A1 PCT/CN2009/070599 CN2009070599W WO2010099645A1 WO 2010099645 A1 WO2010099645 A1 WO 2010099645A1 CN 2009070599 W CN2009070599 W CN 2009070599W WO 2010099645 A1 WO2010099645 A1 WO 2010099645A1
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- polyolefin
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
- C08F255/02—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
Definitions
- the invention belongs to the technical field of polymer polymerization, processing and functionalization, and relates to a coupling method of a polyolefin molecular chain. Background technique
- Polyolefin represented by polypropylene and polyethylene is one of the most widely used thermoplastic polymer materials.
- the softening point of the semi-crystalline polypropylene is very close to the melting point, the melt strength rapidly drops after exceeding the melting point, resulting in a disadvantage of low melt strength and difficulty in blow molding and foaming.
- Polyethylene due to its low melting point, low mechanical strength, and poor environmental stress resistance, limits the application range of polyethylene.
- the coupling treatment of polyethylene is an ideal method to improve the insufficiency of polyethylene.
- the three-dimensional network formed by coupling can greatly improve the thermal deformation, wear, viscous deformation, chemical resistance and stress crack resistance of polyethylene. , the impact and tensile strength of polyethylene are improved, the shrinkage rate is reduced, the use temperature is low, and the like, and the coupled product also has a shape memory function.
- the irradiation cross-linking method is limited by thickness, and has the disadvantages of high cost and limited radiation source.
- the peroxide cross-linking method has low branching rate, easy degradation or excessive cross-linking, and is difficult to stabilize, and the silane cross-linking method exists.
- Water is required as a cross-linking catalyst, which can only be cross-linked after the product is finished. In fact, it lacks other industrial production value except for the pipe. It can be seen that the above three commonly used methods cannot satisfy the long-branched and industrial application of polyolefin.
- Japanese Patent JP6172459 describes a technique for graft-modifying polyolefins by using an olefinic monomer and a peroxide in the presence of a special class of comonomers, which can prevent degradation and cross-linking.
- the combination increases the graft ratio of the vinyl monomer and is used for extrusion molding.
- this patent inhibits the degradation and cross-linking of polyolefins, the graft ratio of the ethylenic monomers is still not sufficiently improved.
- Most of these domestic patents use radiation grafting methods with high cost and poor grafting rate.
- Chinese patents CN1485354 and CN1482151 use radiation grafting to obtain functionalized polyolefin resins.
- Coupling polyolefins used in insulated cables, foamed materials, and thermoplastic elastomers at home and abroad are mostly prepared by peroxide crosslinking, irradiation crosslinking, and silane crosslinking.
- the insulating cable prepared by the oxide cross-linking of Chinese patent CN1300085 reduces the size of the inner spherulites and improves the service life of the cable;
- Japanese patent JP9104052 prepares a drinking water bottle without odor by radiation crosslinking;
- Chinese patent CN1438262 introduces a kind Silane crosslinked polyolefin elastomer composition. Summary of the invention
- the object of the present invention is to provide a coupling of a polyolefin molecular chain capable of producing high-strength long-branched polyolefin, controllable coupling degree, low cost and high productivity, in order to overcome the deficiencies of the prior art mentioned above. method.
- a method for coupling a polyolefin molecular chain characterized in that the method is applied by a solution grafting reaction or a melt grafting reaction in an amount of 0.02 to 10.0 parts by weight of an initiator.
- 0 to 15 parts by weight of the polyfunctional group-containing monomer is grafted with 100 parts by weight of the polyolefin at a certain temperature under the synergistic action of 0 to 15 parts by weight of the second olefin monomer to prepare a side chain.
- a functionalized grafted polyolefin 100 parts by weight of a grafted polyolefin, 0.1 to 20 parts by weight of a polyfunctional organic coupling agent and 0 to 10.0 parts by weight at a certain temperature by solution reaction or melt blending reaction
- the grafting polyolefin is coupled with an antioxidant.
- the polyolefin comprises a copolymer of general-purpose polypropylene, general-purpose polyethylene or ethylene propylene having a melt flow rate of 0.1 g/10 min to 50 g/10 min ; the polyfunctional group-containing monomer comprising acrylic acid, Maleic anhydride, methacrylic acid, fumaric acid, itaconic acid, undecylenic acid, glycidyl methacrylate, acrylamide, N-methylol acrylamide, hydroxyethyl acrylate, hydroxypropyl acrylate
- the second olefin monomers include styrene, divinylbenzene, a-methylstyrene, methyl acrylate, methyl methacrylate, butyl acrylate, butyl methacrylate
- the initiators includes dicumyl peroxide, benzoyl peroxide, dodecyl peroxide, di-tert-butyl peroxide, t
- the solution grafting method comprises the steps of: adding 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight of a polyfunctional group-containing monomer monomer, and 0 to 15 parts by weight of a second olefin monomer to an organic solvent. In the middle, gradually heat up, and stir to form a uniform solution of 5% ⁇ 15%. After removing oxygen by drum nitrogen, gradually add 0.02 ⁇ 10.0 parts by weight of initiator to 3 ⁇ 5 times, and maintain the temperature reaction for 2 ⁇ 4 hours. After the reaction is over, The reaction solution is cooled, the solid is precipitated, filtered, and dried to obtain a grafted polyolefin.
- the organic solvent includes xylene, toluene, trichlorobenzene, chloroform.
- the melt grafting method comprises the steps of: 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight of a polyfunctional group-containing monomer, 0 to 15 parts by weight of a second olefin monomer, and 0.02 to 10.0
- the parts by weight of the initiator are mixed at high speed and then added to a Huck, single screw extruder, twin screw extruder, internal mixer, Banbury mixer or open mill, at 130 ° C ⁇ 250 ° C
- the melt grafting reaction is carried out for 1 min to 30 min, and the product is cooled and pelletized to obtain a graft polyolefin.
- V Formula I R represents the main structure of the polyfunctional coupling agent, and includes an alkyl group, an aryl group, an aralkyl group, an oligomer or an organic structure containing various hetero atoms;
- F representing various functional functional groups, including a carboxyl group, a primary amino group, a secondary amino group, a hydroxyl group, an epoxy group, an isocyanate group, an amide group, a sulfonic acid group, an acid chloride group;
- n represents the number of functional groups, n l.
- the antioxidant includes 2,6-di-tert-butyl-4-ethylphenol, 2,6-di-tert-butyl-4-methylphenol, 2,6-di-tert-butyl-a-dimethyl Amino-p-cresol, 2,4,6-tri-tert-butylphenol, dilauryl thiodipropionate, di(octadecyl) thiodipropionate, di(tetradecyl) thiodipropionate
- One or more of the antioxidant 1010, the antioxidant CA, the antioxidant B215, and the antioxidant B225 are examples of the antioxidant 1010, the antioxidant CA, the antioxidant B215, and the antioxidant B225.
- the solution grafting method comprises the following steps: adding the prepared grafted polyolefin and an antioxidant to a polyolefin solvent, gradually heating up, and stirring to form a uniform solution of 5% to 15%, and removing nitrogen by drum After the oxygen is added, the polyfunctional organic coupling agent is added in one portion, and the temperature is maintained for 0.1 to 1 hour. After the reaction is completed, the reaction solution is cooled, and the solid is precipitated. After filtration and drying, a coupled polyolefin is obtained.
- the polyolefin solvent includes xylene, toluene, trichlorobenzene, chloroform.
- the melt grafting method comprises the following steps: mixing the grafted polyolefin, the antioxidant and the polyfunctional organic coupling agent in a high mixer, and then adding to the Huck, single screw extruder, double In a screw extruder, an internal mixer, a Banbury mixer or an open mill, the melting reaction is carried out at 130 ° C to 250 ° C for 1 min to 30 min, and the product is cooled and pelletized to obtain a coupled polymer. Olefins.
- the present invention reacts the polyfunctional group-containing monomer with the polyolefin by the synergistic action of the second olefin monomer by the solution grafting reaction or the melt grafting reaction under the action of the initiator.
- the grafting reaction is carried out at a certain temperature to prepare a graft polyolefin having a functional group in a side chain.
- the grafted polyolefin prepared is then coupled to a coupled, long-branched polyolefin by a solution reaction or a melt reaction using a polyfunctional organic coupling agent at a temperature.
- Polyolefins of various coupling degrees can be prepared according to different use requirements, and the coupled polyolefin prepared by the method can be widely used for foaming materials, pipes, cables, thermoplastic elastomers, beverage bottles, and plates. detailed description
- the grafting ratio of the polyfunctional olefinic monomer of the grafted polyolefin obtained by infrared spectroscopy was measured, and the relative intensity of the characteristic peaks before and after the extraction was measured. According to Lambert Beer's law, the reaction efficiency was determined.
- the calculation formula is:
- the MFR was measured using a SRSY-1 melt flow rate meter at 230 ° C under a load of 2.16 kg.
- the PP sample was placed in a vacuum tableting machine at a temperature of 200 ° C, pressed for 30 min, and a sheet having a thickness of about 1 mm was prepared, and then the storage mold was tested by a Rheostress 600 rheometer manufactured by Thermo Haake.
- the long-branched polyolefin prepared by the polyolefin coupling method of the present invention is composed of a specific amount of polyolefin resin, a specific amount of A functional group of an olefinic monomer, a specific amount of a second olefin monomer, and a specific amount of an initiator obtain a polyolefin having a side chain functional group by solution or melt grafting reaction. It is then obtained by solution or melt chemical reaction using a specific amount of a polyfunctional organic coupling agent and a specific amount of an antioxidant.
- the materials and amounts used for the coupled polyolefin prepared by the polyolefin coupling method of the present invention are as follows:
- a polyolefin resin including a copolymer of polypropylene, polyethylene or ethylene propylene, having a melt flow rate of between 0.1 g/10 min and 50 g/10 min, preferably melting
- the body flow rate is lg/10 min to 30 g/10 min.
- the melt flow rate is too large or too small, which is unfavorable for the reaction of the polyolefin resin with the polyfunctional olefin-containing monomer, thereby lowering the reaction efficiency and affecting the branching rate of the final coupled polyolefin. Therefore, a further preferred polyolefin melt flow rate is from 3 g/10 min to 20 g/10 min.
- a polyfunctional olefinic monomer including acrylic acid, maleic anhydride, methacrylic acid, fumaric acid, itaconic acid, undecylenic acid, methyl One or more of glycidyl acrylate, acrylamide, N-methylol acrylamide, hydroxyethyl acrylate, and hydroxypropyl acrylate.
- the amount of addition is preferably 2 to 18 parts, more preferably 3 to 12 parts. 1 ⁇ , if the amount of the polyfunctional monomer is less than 0.1 part, the amount of the polyfunctional monomer is less than 0.1 part, It is difficult to achieve the purpose of coupling.
- the second olefin monomer including methyl acrylate, methyl methacrylate, butyl acrylate, butyl methacrylate, styrene, divinylbenzene, a-A One or several kinds of styrene.
- the amount of addition is preferably 2 to 18 parts, more preferably 3 to 12 parts.
- the addition of the olefin monomer can, on the one hand, increase the reaction efficiency of the polyfunctional group-containing monomer and, on the other hand, inhibit the degradation of the polyolefin. However, if the amount of the olefin monomer is more than 25 parts, the second olefin monomer will produce more homopolymer, which affects the performance of the coupled polyolefin.
- an initiator including dicumyl peroxide, benzoyl peroxide, dodecyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, Peroxide initiator such as t-butyl peroxybenzoate, 1, 4-bis(tert-butylperoxyisopropyl)benzene, and azo One or more of diisobutyl phthalate, azo diisoheptane, and the like.
- an initiator including dicumyl peroxide, benzoyl peroxide, dodecyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, Peroxide initiator such as t-butyl peroxybenzoate, 1, 4-bis(tert-butylperoxyisopropyl)benzene, and azo One or more of diisobutyl phthalate, azo diisoheptane, and the like.
- the amount of the initiator is less than 0.02 part by weight, the concentration of the radical generated is too low, which lowers the reaction efficiency of the polyfunctional ethylenic monomer and the polyolefin, and affects the use properties of the coupled polyolefin.
- the amount of the initiator is more than 10.0 parts by weight, serious crosslinking and degradation of the polyolefin may be caused, and in addition, the residual initiator may deteriorate the properties of the coupled polyolefin.
- the grafting reaction of the polyolefin can be carried out by a solution reaction and a melt reaction: the solution reaction is carried out by adding various materials other than the initiator to an organic solvent such as xylene, toluene, trichlorobenzene or chloroform. Gradually raise the temperature to 100 to 145 degrees and stir to form a uniform solution of 5% to 15%. After the nitrogen gas is removed from the drum, the initiator is gradually added in 3 to 5 times, and the temperature is maintained for 2 to 4 hours. After completion of the reaction, the reaction solution was cooled, and a solid precipitated, which was filtered and dried to obtain a graft polyolefin.
- an organic solvent such as xylene, toluene, trichlorobenzene or chloroform. Gradually raise the temperature to 100 to 145 degrees and stir to form a uniform solution of 5% to 15%. After the nitrogen gas is removed from the drum, the initiator is gradually added in 3 to 5 times, and the temperature is maintained
- the reaction temperature is lower than ioo °c, the polyolefin may be incompletely dissolved, making the grafting reaction difficult. If the reaction temperature is too high, the solvent is vigorously boiled so that the grafting reaction cannot be stably carried out.
- the melt reaction is carried out by mixing various materials at high speed and then adding them to a Huck, a single screw extruder, a twin screw extruder, an internal mixer, a Banbury mixer, and an open mill at 130 ° C to 250 °.
- the melting reaction is carried out in the range of C, and it is more preferable to carry out the melting reaction in the range of from 120 ° C to 200 ° C, and the reaction time is from 1 min to 30 min, more preferably from 3 min to 8 min.
- the product is cooled and pelletized to obtain a grafted polyolefin.
- the reaction temperature is lower than 100 °C, the polyolefin cannot be completely melted, and the graft reaction is difficult to proceed. If the reaction temperature is higher than 250 °C, not only will the graft ratio of the polyolefin be lowered, but also the polyolefin product will be degraded and its physical properties deteriorated. If the reaction time is less than 1 min, the grafting reaction does not proceed completely, affecting the graft ratio of the polyolefin, and the residual initiator may deteriorate the properties of the polyolefin product. If the reaction time is more than 30 minutes, it is possible to degrade the polyolefin.
- R represents the main structure of the polyfunctional coupling agent, such as an alkyl group, an aryl group, an aralkyl group, an oligomer or an organic structure containing various hetero atoms.
- the solution reaction it is preferred to use an organic substance in which R is an alkyl group; for the melt blending reaction, it is preferred that R is an oligomer or an aralkyl organic substance, which can enhance the compatibility of the polyfunctional organic coupling agent with the grafted polyolefin. , the coupling reaction proceeds smoothly.
- F representing various functional functional groups, such as a carboxyl group, a primary amino group, a secondary amino group, a hydroxyl group, an epoxy group, an isocyanate group, an amide group, a sulfonic acid group, an acid chloride group, etc., preferably using F as a primary amino group or a carboxyl group.
- the functional group it is further preferred to use a functional group in which F is a primary amino group, which accelerates the reaction rate of the polyfunctional organic group with the grafted polyolefin.
- antioxidant content including 2,6-di-tert-butyl-4-ethylphenol, 2,6-di-tert-butyl-4-methylphenol, 2, 6-di-tert-butyl- ⁇ -dimethylamino-p-cresol, 2,4,6-tri-tert-butylphenol, dilauryl thiodipropionate, di(octadecyl) thiodipropionate, One or more of di(tetradecyl thiodipropionate), antioxidant 1010, antioxidant CA, antioxidant B215, and antioxidant B225.
- the addition of the antioxidant can adjust the reaction state and melt flowability of the coupled polyolefin, but if it is added in an amount of more than 10 parts, the use properties of the coupled polyolefin are deteriorated.
- the coupling of the grafted polyolefin can be generally carried out by the following two methods, thereby obtaining the coupled polyolefin of the present invention.
- Solution reaction method According to the above-mentioned ingredients, the grafted polyolefin prepared according to the above method is added to an organic solvent such as xylene, toluene, trichlorobenzene, chloroform, etc., and gradually heated, and stirred to form 5% ⁇ 15% homogeneous solution. After the nitrogen is removed from the drum, the polyfunctional organic substance is added to the solution at a time, and the temperature is maintained for 0.5 to 1 hour. After completion of the reaction, the reaction solution was cooled, and a solid precipitated, which was filtered and dried to obtain a coupled polyolefin.
- an organic solvent such as xylene, toluene, trichlorobenzene, chloroform, etc.
- Examples and Comparative Examples 1 to 2 are preparations of long-branched polypropylene in solution:
- Example 1 Polypropylene EPS30R (Qilu Petrochemical Co., Ltd.) 100 g, 1010 antioxidant 0.1 g, was added to a 2000 ml flask, and then 1300 g of xylene was added thereto, and the temperature was gradually raised to 140 °C. After the solid was completely dissolved, 2 g of an acrylic graft monomer, 2 g of styrene was added, and then 0.36 g of benzoyl peroxide was added to the flask 5 times in 30 minutes to maintain the reaction at 140 °C.
- Comparative Example 1 50 g of the grafted polypropylene prepared in Example 1 was taken.
- the grafting method of the grafted polypropylene was the same as in Example 1, except that 1.2 g of ethylene glycol diglycidyl ether was added as a coupling agent to the grafted polypropylene solution for coupling reaction.
- the properties of the obtained long-branched polypropylene are shown in Table 1.
- Example 2 The polypropylene grafting method was the same as in Example 1, except that glycolic acid methacrylate was grafted with polypropylene as a grafting monomer.
- the coupling method was also the same as in Example 1, except that 0.65 g of hexamethylene diisocyanate (HDI) was added as a coupling agent to the grafted polypropylene solution for the coupling reaction.
- HDI hexamethylene diisocyanate
- Comparative Example 2 50 g of the grafted polypropylene prepared in Example 2 was taken.
- the coupling method of the grafted polypropylene was the same as in Example 1, except that 0.67 g of toluene-2,4-diisocyanate (TDI) was added as a coupling agent to the grafted polypropylene solution for coupling reaction.
- TDI toluene-2,4-diisocyanate
- Examples and Comparative Examples 3 to 4 are preparations of long-branched polypropylene by a melt method:
- Example 3 Take polypropylene EPS30R (Qilu Petrochemical Co., Ltd.) 10 kg, GMA graft monomer 0.2 kg, styrene 0.2 kg, dicumyl peroxide 36 g, dissolve dicumyl peroxide in GMA And styrene monomer, and then all mixed in a high-speed mixer for 2 minutes, discharging. The mixture was added to a twin-screw extruder which had been preheated to 170 ° C, and the reaction was extruded at 50 rpm. The extruded product is pelletized to obtain a grafted polyolefin. The grafting ratio results of GMA and polyolefin are shown in Table 1.
- Comparative Example 3 5 kg of the grafted polypropylene prepared in Example 3 was taken.
- the coupling method of the grafted polypropylene was the same as in Example 3 except that 3 1.0 g of butanediamine was added as a coupling agent to the grafted polypropylene for the coupling reaction.
- the properties of the obtained long-branched polypropylene are shown in Table 2.
- Example 4 Its polypropylene grafting method was the same as in Example 3 except that maleic anhydride was grafted with polypropylene as a grafting monomer.
- the coupling method was also the same as in Example 3 except that 74.5 g of octanediol was added as a coupling agent to the grafted polypropylene for coupling reaction.
- Table 2 The results of the graft ratio of maleic anhydride to polypropylene and the properties of the obtained long-branched polyolefin are shown in Table 2.
- Comparative Example 4 5 kg of the grafted polypropylene prepared in Example 4 was taken.
- the coupling method of the grafted polypropylene was the same as in Example 4 except that 32.7 g of ethylene glycol was added as a coupling agent to the grafted polypropylene for the coupling reaction.
- the properties of the obtained long-branched polypropylene are shown in Table 2.
- both acrylic acid and hydroxyethyl methacrylate can be grafted with polypropylene, and the graft ratio is relatively high, and the graft ratio of hydroxyethyl methacrylate to acrylic acid is higher. This may be because hydroxyethyl methacrylate is more compatible with polypropylene than acrylic acid.
- the long-branched polypropylene coupled with 1,4 butanediol diglycidyl ether and HDI has a lower melt flow rate than EPS30R, and the storage modulus is higher than EPS30R, indicating that after the coupling of the two coupling agents The polypropylene is effectively branched.
- the performance of polypropylene coupled with ethylene glycol diglycidyl ether and TDI was deteriorated. This is because the latter two coupling agents have a relatively short molecular chain and are embedded in the molecular chain of the polypropylene during the coupling reaction, resulting in a failure of the coupling reaction.
- the longer coupling agent can carry out the coupling reaction between different polypropylene molecular chains to cause the polypropylene to be branched.
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Abstract
Method for coupling polyolefin chains includes solution grafting or melt grafting polyolefin (100 pts. wt.) with a polyfunctional-containing alkene monomer (0-15 pts. wt.) in the presence of a second alkene monomer (0-15 pts. wt.) and an initiator (0.02-10.0 pts. wt.) at a determined temperature to obtain grafted polyolefin with a side chain comprising functional groups; then, by means of a solution-grafting or a melt-blending reaction, adding a polyfunctional organic coupling agent (0.1-20 pts. wt.) and an antioxidant (0-10.0 pts. wt.) to said grafted polyolefin (100 pts. wt.) at a specific temperature to obtain coupled polyolefin. Compared to the art, the method produces high-strength long-branched polyolefin with a controllable degree of coupling, at low cost and high production rates.
Description
一种聚烯烃分子链的偶联方法 Method for coupling polyolefin molecular chain
技术领域 Technical field
本发明属于聚合物聚合、 加工以及功能化技术领域, 涉及一种聚烯烃分 子链的偶联方法。 背景技术 The invention belongs to the technical field of polymer polymerization, processing and functionalization, and relates to a coupling method of a polyolefin molecular chain. Background technique
以聚丙烯、 聚乙烯为代表的聚烯烃是应用最为广泛的热塑性高分子材料 之一。 但是, 由于半结晶的聚丙烯软化点与熔点很接近, 超过熔点后其熔体 强度迅速下降, 从而导致其熔体强度低和难以吹塑和发泡的缺点。 而聚乙烯 又因其熔点较低、 机械强度不高、 耐环境应力性能较差等缺点, 限制了聚乙 烯的应用范围。 通过偶联改性可以降低聚丙烯的热收缩率, 提高聚丙烯的冲 击强度, 扩大其应用的范围。 对聚乙烯进行偶联处理是改进聚乙烯不足之处 的理想方法, 经偶联, 形成的三维网络可大大改善聚乙烯的热变形、 磨损、 粘性变形、 耐化学性、 耐应力开裂性等性能, 使聚乙烯的冲击和拉伸强度提 高, 收缩率减小, 使用温度低等不足得到改善, 而且偶联产品还有形状记忆 功能。 Polyolefin represented by polypropylene and polyethylene is one of the most widely used thermoplastic polymer materials. However, since the softening point of the semi-crystalline polypropylene is very close to the melting point, the melt strength rapidly drops after exceeding the melting point, resulting in a disadvantage of low melt strength and difficulty in blow molding and foaming. Polyethylene, due to its low melting point, low mechanical strength, and poor environmental stress resistance, limits the application range of polyethylene. By coupling modification, the heat shrinkage of polypropylene can be reduced, the impact strength of polypropylene can be increased, and the range of application can be expanded. The coupling treatment of polyethylene is an ideal method to improve the insufficiency of polyethylene. The three-dimensional network formed by coupling can greatly improve the thermal deformation, wear, viscous deformation, chemical resistance and stress crack resistance of polyethylene. , the impact and tensile strength of polyethylene are improved, the shrinkage rate is reduced, the use temperature is low, and the like, and the coupled product also has a shape memory function.
聚烯烃偶联方法主要有三种: 过氧化物交联、 辐照交联和硅烷交联。 辐 照交联法受到厚度限制, 存在成本高、 辐射源有限等缺点; 过氧化物交联法 存在枝化率低, 易降解或过度交联, 难以稳定等缺陷, 而硅烷交联法又存在 需用水作交联剂催化剂, 只能在完成制品后再交联, 实际上除作管材外缺乏 其它工业生产价值。 可见以上三种常用的方法不能满足聚烯烃的长枝化化及 工业化应用。 There are three main types of polyolefin coupling methods: peroxide crosslinking, irradiation crosslinking, and silane crosslinking. The irradiation cross-linking method is limited by thickness, and has the disadvantages of high cost and limited radiation source. The peroxide cross-linking method has low branching rate, easy degradation or excessive cross-linking, and is difficult to stabilize, and the silane cross-linking method exists. Water is required as a cross-linking catalyst, which can only be cross-linked after the product is finished. In fact, it lacks other industrial production value except for the pipe. It can be seen that the above three commonly used methods cannot satisfy the long-branched and industrial application of polyolefin.
以中国专利 CN 1380344为例, 它介绍了一种聚烯烃塑料熔融接枝烯类单 体的力化学方法, 将烯类单体、 润滑剂和聚烯烃混合后加入带有超声波发生 器和超声波传感器的挤出机内, 进行连续挤出接枝反应, 获得聚烯烃接枝聚 合物或者共聚物。 但是此专利一方面所用的设备比较复杂, 另外使用的聚烯 烃必须是聚乙烯或者含有乙烯链段的共聚物, 从而限制了在聚丙烯方面的应 用,而且接枝率较低。日本专利 JP6172459介绍了在一类特殊的共单体存在下, 通过烯类单体和过氧化物进行接枝改性聚烯烃的技术, 可以在防止降解和交
联的同时提高烯类单体的接枝率以及用于挤出模塑。 此专利虽然抑制了聚烯 烃的降解和交联, 但是烯类单体的接枝率仍然不能得到足够的提高。 而国内 的此类专利大都是采用成本高、 接枝率不易控制的辐射接枝的方法, 例如中 国专利 CN1485354和 CN1482151都是采用辐射接枝的方法获得功能化聚烯烃 树脂。 Taking Chinese patent CN 1380344 as an example, it introduces a force chemistry method for melt-grafting vinyl monomers of polyolefin plastics, mixing vinyl monomers, lubricants and polyolefins with ultrasonic generators and ultrasonic sensors. In the extruder, a continuous extrusion grafting reaction is carried out to obtain a polyolefin graft polymer or copolymer. However, the apparatus used on the one hand is complicated, and the polyolefin used must be polyethylene or a copolymer containing ethylene segments, thereby limiting the application in polypropylene and having a low grafting ratio. Japanese Patent JP6172459 describes a technique for graft-modifying polyolefins by using an olefinic monomer and a peroxide in the presence of a special class of comonomers, which can prevent degradation and cross-linking. The combination increases the graft ratio of the vinyl monomer and is used for extrusion molding. Although this patent inhibits the degradation and cross-linking of polyolefins, the graft ratio of the ethylenic monomers is still not sufficiently improved. Most of these domestic patents use radiation grafting methods with high cost and poor grafting rate. For example, Chinese patents CN1485354 and CN1482151 use radiation grafting to obtain functionalized polyolefin resins.
国内外在绝缘电缆、 发泡材料和热塑性弹性体等方面使用的偶联聚烯烃 大都是使用过氧化物交联、 辐照交联和硅烷交联来制备的。 如中国专利 CN1300085通过氧化物交联制备的绝缘电缆降低了内部球晶的尺寸并且提高 了电缆的使用寿命; 日本专利 JP9104052通过辐射交联制备了没有异味的饮 水瓶; 中国专利 CN1438262介绍了一种硅烷交联聚烯烃弹性体组合物。 发明内容 Coupling polyolefins used in insulated cables, foamed materials, and thermoplastic elastomers at home and abroad are mostly prepared by peroxide crosslinking, irradiation crosslinking, and silane crosslinking. For example, the insulating cable prepared by the oxide cross-linking of Chinese patent CN1300085 reduces the size of the inner spherulites and improves the service life of the cable; Japanese patent JP9104052 prepares a drinking water bottle without odor by radiation crosslinking; Chinese patent CN1438262 introduces a kind Silane crosslinked polyolefin elastomer composition. Summary of the invention
本发明的目的就是为了克服上述现有技术存在的不足之处而提供一种 可以生产高强度的长枝化聚烯烃, 偶联度可控, 成本低廉, 生产率高的聚烯 烃分子链的偶联方法。 The object of the present invention is to provide a coupling of a polyolefin molecular chain capable of producing high-strength long-branched polyolefin, controllable coupling degree, low cost and high productivity, in order to overcome the deficiencies of the prior art mentioned above. method.
本发明的目的可以通过以下技术方案来实现: 一种聚烯烃分子链的偶联 方法, 其特征在于, 该方法通过溶液接枝反应或者熔融接枝反应, 在 0.02〜 10.0重量份引发剂的作用下, 使 0〜 15重量份含多官能团的烯类单体在 0〜 15 重量份第二烯烃单体协同作用下与 100重量份聚烯烃在一定温度下进行接枝 反应, 制备侧链带有官能团的接枝聚烯烃; 取 100重量份的接枝聚烯烃, 通 过溶液反应或者熔融共混反应,在一定温度下加入 0.1〜20重量份的多官能团 有机偶联剂和 0〜 10.0重量份的抗氧剂将所述接枝聚烯烃进行偶联。 The object of the present invention can be achieved by the following technical solutions: A method for coupling a polyolefin molecular chain, characterized in that the method is applied by a solution grafting reaction or a melt grafting reaction in an amount of 0.02 to 10.0 parts by weight of an initiator. Next, 0 to 15 parts by weight of the polyfunctional group-containing monomer is grafted with 100 parts by weight of the polyolefin at a certain temperature under the synergistic action of 0 to 15 parts by weight of the second olefin monomer to prepare a side chain. a functionalized grafted polyolefin; 100 parts by weight of a grafted polyolefin, 0.1 to 20 parts by weight of a polyfunctional organic coupling agent and 0 to 10.0 parts by weight at a certain temperature by solution reaction or melt blending reaction The grafting polyolefin is coupled with an antioxidant.
所述的聚烯烃包括通用聚丙烯、 通用聚乙烯或乙烯丙烯的共聚物, 其熔 体流动速率为 0.1g/10min〜50 g/10min; 所述的含多官能团的烯类单体包括丙 烯酸、 马来酸酐、 甲基丙烯酸、 富马酸、 衣康酸、 十一碳烯酸、 甲基丙烯酸 缩水甘油酯、 丙烯酰胺、 N-羟甲基丙烯酰胺、 丙烯酸羟乙酯、 丙烯酸羟丙酯 中的一种或者几种; 所述的第二烯烃单体包括苯乙烯、 二乙烯基苯、 a -甲基 苯乙烯、 丙烯酸甲酯、 甲基丙烯酸甲酯、 丙烯酸丁酯、 甲基丙烯酸丁酯中的 一种或几种; 所述的引发剂包括过氧化二异丙苯、 过氧化苯甲酰、 过氧化十 二酰、 二叔丁基过氧化物、 叔丁基过氧化氢、 叔丁基过氧化苯甲酸酯、 1,
4-双 (叔丁基过氧化异丙基) 苯, 或者偶氮二异丁睛、 偶氮二异庚睛中的一 种或者几种。 The polyolefin comprises a copolymer of general-purpose polypropylene, general-purpose polyethylene or ethylene propylene having a melt flow rate of 0.1 g/10 min to 50 g/10 min ; the polyfunctional group-containing monomer comprising acrylic acid, Maleic anhydride, methacrylic acid, fumaric acid, itaconic acid, undecylenic acid, glycidyl methacrylate, acrylamide, N-methylol acrylamide, hydroxyethyl acrylate, hydroxypropyl acrylate One or more of the second olefin monomers include styrene, divinylbenzene, a-methylstyrene, methyl acrylate, methyl methacrylate, butyl acrylate, butyl methacrylate One or more of the initiators; the initiator includes dicumyl peroxide, benzoyl peroxide, dodecyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, tert-butyl Base benzoate, 1, 4-bis(tert-butylperoxyisopropyl)benzene, or one or more of azobisisobutyronitrile and azobishesin.
所述的溶液接枝法包括如下步骤: 将 100重量份的聚烯烃树脂、 0〜15重 量份的含多官能团的烯类单体和 0〜 15重量份的第二烯烃单体加入到有机溶 剂中, 逐步升温, 并搅拌, 形成 5%〜15%的均匀溶液, 鼓氮气排除氧气后, 分 3〜5次逐步加入 0.02〜10.0重量份引发剂, 维持温度反应 2〜4小时, 反应 结束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到接枝聚烯烃。 The solution grafting method comprises the steps of: adding 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight of a polyfunctional group-containing monomer monomer, and 0 to 15 parts by weight of a second olefin monomer to an organic solvent. In the middle, gradually heat up, and stir to form a uniform solution of 5%~15%. After removing oxygen by drum nitrogen, gradually add 0.02~10.0 parts by weight of initiator to 3~5 times, and maintain the temperature reaction for 2~4 hours. After the reaction is over, The reaction solution is cooled, the solid is precipitated, filtered, and dried to obtain a grafted polyolefin.
所述的有机溶剂包括二甲苯、 甲苯、 三氯苯、 氯仿。 The organic solvent includes xylene, toluene, trichlorobenzene, chloroform.
所述的熔融接枝法包括如下步骤: 将 100重量份的聚烯烃树脂、 0〜15重 量份的含多官能团的烯类单体、 0〜15重量份的第二烯烃单体和 0.02〜10.0重 量份引发剂经高速混合后加入到哈克、 单螺杆挤出机、 双螺杆挤出机、 密炼 机、 班伯里混合机或开炼机中, 于 130°C〜250°C下进行熔融接枝反应, 反应 lmin〜30min, 将产物冷却、 切粒, 制得接枝聚烯烃。 The melt grafting method comprises the steps of: 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight of a polyfunctional group-containing monomer, 0 to 15 parts by weight of a second olefin monomer, and 0.02 to 10.0 The parts by weight of the initiator are mixed at high speed and then added to a Huck, single screw extruder, twin screw extruder, internal mixer, Banbury mixer or open mill, at 130 ° C ~ 250 ° C The melt grafting reaction is carried out for 1 min to 30 min, and the product is cooled and pelletized to obtain a graft polyolefin.
所述的多官能团有机偶联剂的结构式如式 I: The structural formula of the polyfunctional organic coupling agent is as shown in formula I:
V 式 I R, 代表多官能团偶联剂的主要结构, 包括烷基、 芳基、 芳烷基、 齐聚 物或者含有各种杂原子的有机结构; V Formula I R represents the main structure of the polyfunctional coupling agent, and includes an alkyl group, an aryl group, an aralkyl group, an oligomer or an organic structure containing various hetero atoms;
F, 代表各种功能性官能团, 包括羧基、 伯胺基、 仲胺基、 羟基、 环氧 基、 异氰酸酯基、 酰胺基、 磺酸基、 酰氯基; F, representing various functional functional groups, including a carboxyl group, a primary amino group, a secondary amino group, a hydroxyl group, an epoxy group, an isocyanate group, an amide group, a sulfonic acid group, an acid chloride group;
n , 代表官能团的个数, n l。 n , represents the number of functional groups, n l.
所述的抗氧剂包括 2, 6-二叔丁基 -4-乙基苯酚、 2, 6-二叔丁基 -4-甲基苯 酚、 2, 6-二叔丁基 - a -二甲氨基-对甲酚、 2, 4, 6-三叔丁基苯酚、 硫代二丙 酸二月桂酯、 硫代二丙酸二 (十八酯) 、 硫代二丙酸二 (十四酯) 、 抗氧剂 1010、 抗氧剂 CA、 抗氧剂 B215以及抗氧剂 B225中的一种或几种。 The antioxidant includes 2,6-di-tert-butyl-4-ethylphenol, 2,6-di-tert-butyl-4-methylphenol, 2,6-di-tert-butyl-a-dimethyl Amino-p-cresol, 2,4,6-tri-tert-butylphenol, dilauryl thiodipropionate, di(octadecyl) thiodipropionate, di(tetradecyl) thiodipropionate One or more of the antioxidant 1010, the antioxidant CA, the antioxidant B215, and the antioxidant B225.
所述的溶液接枝法包括如下步骤: 将制备的接枝聚烯烃和抗氧剂加入到 聚烯烃溶剂中, 逐步升温, 并搅拌, 形成 5%〜15%的均匀溶液, 鼓氮气排除
氧气后, 一次性加入含多官能团的有机偶联剂, 维持温度反应 0. 1〜1小时, 反应结束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到偶联聚烯烃。 The solution grafting method comprises the following steps: adding the prepared grafted polyolefin and an antioxidant to a polyolefin solvent, gradually heating up, and stirring to form a uniform solution of 5% to 15%, and removing nitrogen by drum After the oxygen is added, the polyfunctional organic coupling agent is added in one portion, and the temperature is maintained for 0.1 to 1 hour. After the reaction is completed, the reaction solution is cooled, and the solid is precipitated. After filtration and drying, a coupled polyolefin is obtained.
所述的聚烯烃溶剂包括二甲苯、 甲苯、 三氯苯、 氯仿。 The polyolefin solvent includes xylene, toluene, trichlorobenzene, chloroform.
所述的熔融接枝法包括如下步骤: 将接枝聚烯烃、 抗氧剂和含多官能团 的有机偶联剂在高混机中混合均匀, 然后加入到哈克、 单螺杆挤出机、 双螺 杆挤出机、 密炼机、 班伯里混合机或开炼机中, 于 130 °C〜250 °C下进行熔融 反应, 反应 lmin〜30min, 将产物冷却、 切粒, 制得偶联聚烯烃。 The melt grafting method comprises the following steps: mixing the grafted polyolefin, the antioxidant and the polyfunctional organic coupling agent in a high mixer, and then adding to the Huck, single screw extruder, double In a screw extruder, an internal mixer, a Banbury mixer or an open mill, the melting reaction is carried out at 130 ° C to 250 ° C for 1 min to 30 min, and the product is cooled and pelletized to obtain a coupled polymer. Olefins.
与现有技术相比, 本发明通过溶液接枝反应或者熔融接枝反应, 在引发 剂的作用下, 使含多官能团的烯类单体在第二烯烃单体的协同作用下与聚烯 烃在一定温度下进行接枝反应, 制备侧链带有官能团的接枝聚烯烃。 然后通 过溶液反应或者熔融反应, 在一定温度下利用多官能团的有机偶联剂令所制 备的接枝聚烯烃偶联得到偶联的、 长枝化的聚烯烃。 用这种方法可以生产高 强度的长枝化聚烯烃, 其偶联度可控, 成本低廉, 生产率高。 可以按照不同 的使用要求制备各种偶联度的聚烯烃, 用该方法制备的偶联聚烯烃可以广泛 使用于发泡材料、 管材、 电缆、 热塑性弹性体、 饮料瓶以及板材等。 具体实施方式 Compared with the prior art, the present invention reacts the polyfunctional group-containing monomer with the polyolefin by the synergistic action of the second olefin monomer by the solution grafting reaction or the melt grafting reaction under the action of the initiator. The grafting reaction is carried out at a certain temperature to prepare a graft polyolefin having a functional group in a side chain. The grafted polyolefin prepared is then coupled to a coupled, long-branched polyolefin by a solution reaction or a melt reaction using a polyfunctional organic coupling agent at a temperature. In this way, high-strength long-branched polyolefins can be produced with controlled coupling, low cost, and high productivity. Polyolefins of various coupling degrees can be prepared according to different use requirements, and the coupled polyolefin prepared by the method can be widely used for foaming materials, pipes, cables, thermoplastic elastomers, beverage bottles, and plates. detailed description
接枝聚烯烃中多官能团烯类单体接枝率的测定 Determination of grafting rate of polyfunctional olefinic monomers in grafted polyolefins
采用红外光谱测试所得到的接枝聚烯烃的含多官能团烯类单体接枝率, 测定其萃取前后特征峰的相对强度, 根据朗伯比尔定律, 可求出反应效率。 计算公式为: The grafting ratio of the polyfunctional olefinic monomer of the grafted polyolefin obtained by infrared spectroscopy was measured, and the relative intensity of the characteristic peaks before and after the extraction was measured. According to Lambert Beer's law, the reaction efficiency was determined. The calculation formula is:
反应效率= 100%*C2/ d-d ) Reaction efficiency = 100% * C 2 / dd )
其中, 配比中多官能团接枝单体的浓度; Wherein the concentration of the polyfunctional grafting monomer in the ratio;
c2 萃取后多官能团接枝单体的浓度 Concentration of polyfunctional grafting monomer after c 2 extraction
1 - d 萃取前聚烯烃的浓度, 即为聚烯烃的初始投料量。 1 - d The concentration of the polyolefin before extraction, which is the initial charge of the polyolefin.
偶联聚烯烃熔体流动速率 (MFR) 的测定 Determination of melt flow rate (MFR) of coupled polyolefin
MFR用 SRSY- 1熔体流动速率测定仪在 230 °C, 2. 16kg载荷下测定。 The MFR was measured using a SRSY-1 melt flow rate meter at 230 ° C under a load of 2.16 kg.
偶联聚烯烃储能模量的测定 Determination of storage modulus of coupled polyolefin
PP样品置于温度 200°C的真空压片机中, 压片 30min, 制成厚度约为 lmm 的薄片, 然后用 Thermo Haake生产的 Rheostress600流变分析仪测试其储能模
下面实施例是对本发明的进一步说明, 而不是限制本发明的范围: 本发明所述的聚烯烃偶联方法制备的长枝化聚烯烃, 是由特定量的聚烯 烃树脂, 特定量的含多官能团的烯类单体, 特定量的第二烯烃单体, 特定量 的引发剂通过溶液或熔融接枝反应得到含有侧链官能团的聚烯烃。 然后再利 用特定量的含多官能团的有机偶联剂和特定量的抗氧剂, 通过溶液或熔融化 学反应的方法而得到。 The PP sample was placed in a vacuum tableting machine at a temperature of 200 ° C, pressed for 30 min, and a sheet having a thickness of about 1 mm was prepared, and then the storage mold was tested by a Rheostress 600 rheometer manufactured by Thermo Haake. The following examples are illustrative of the invention and are not intended to limit the scope of the invention: The long-branched polyolefin prepared by the polyolefin coupling method of the present invention is composed of a specific amount of polyolefin resin, a specific amount of A functional group of an olefinic monomer, a specific amount of a second olefin monomer, and a specific amount of an initiator obtain a polyolefin having a side chain functional group by solution or melt grafting reaction. It is then obtained by solution or melt chemical reaction using a specific amount of a polyfunctional organic coupling agent and a specific amount of an antioxidant.
使用本发明所述的聚烯烃偶联方法制备的偶联聚烯烃所采用的原料和 用量如下: The materials and amounts used for the coupled polyolefin prepared by the polyolefin coupling method of the present invention are as follows:
( 1 ) 100份 (重量份数) 的聚烯烃树脂, 包括聚丙烯、 聚乙烯或乙烯丙 烯的共聚物, 其熔体流动速率在 0. 1g/10min〜50 g/10min之间, 优选的熔体流 动速率为 lg/10min〜30 g/10min。熔体流动速率太大或太小, 都不利于聚烯烃 树脂与含多官能团的烯类单体的反应, 从而降低反应效率, 影响最终的偶联 聚烯烃的枝化率。 所以, 进一步优选的聚烯烃熔体流动速率为 3g/10min〜20 g/10min。 (1) 100 parts by weight of a polyolefin resin, including a copolymer of polypropylene, polyethylene or ethylene propylene, having a melt flow rate of between 0.1 g/10 min and 50 g/10 min, preferably melting The body flow rate is lg/10 min to 30 g/10 min. The melt flow rate is too large or too small, which is unfavorable for the reaction of the polyolefin resin with the polyfunctional olefin-containing monomer, thereby lowering the reaction efficiency and affecting the branching rate of the final coupled polyolefin. Therefore, a further preferred polyolefin melt flow rate is from 3 g/10 min to 20 g/10 min.
( 2 ) 0. 1〜25份 (重量份) 的含多官能团的烯类单体, 包括丙烯酸、 马 来酸酐、 甲基丙烯酸、 富马酸、 衣康酸、 十一碳烯酸、 甲基丙烯酸缩水甘油 酯、 丙烯酰胺、 N-羟甲基丙烯酰胺、 丙烯酸羟乙酯、 丙烯酸羟丙酯中的一种 或者几种。 添加量优选为 2〜18份, 进一步优选为 3〜12份。 如果接枝单体的 用量大于 25份, 会使接枝单体之间产生较多的均聚物, 影响偶联聚烯烃的性 能; 但如果多官能团单体的添加量小于 0. 1份, 则难以达到偶联的目的。 (2) 0.1 to 25 parts by weight of a polyfunctional olefinic monomer, including acrylic acid, maleic anhydride, methacrylic acid, fumaric acid, itaconic acid, undecylenic acid, methyl One or more of glycidyl acrylate, acrylamide, N-methylol acrylamide, hydroxyethyl acrylate, and hydroxypropyl acrylate. The amount of addition is preferably 2 to 18 parts, more preferably 3 to 12 parts. 1份, if the amount of the polyfunctional monomer is less than 0.1 part, the amount of the polyfunctional monomer is less than 0.1 part, It is difficult to achieve the purpose of coupling.
( 3 ) 0〜25份 (重量份) 的第二烯烃单体, 包括丙烯酸甲酯、 甲基丙烯 酸甲酯、 丙烯酸丁酯、 甲基丙烯酸丁酯、 苯乙烯、 二乙烯基苯、 a -甲基苯乙 烯的一种或几种。 添加量优选为 2〜18份, 进一步优选为 3〜12份。 加入烯烃 单体一方面可以提高含多官能团的烯类单体的反应效率, 另一方面可以抑制 聚烯烃的降解。 但如果烯烃单体的用量大于 25份, 会使第二烯烃单体产生较 多的均聚物, 影响偶联聚烯烃的性能。 (3) 0 to 25 parts by weight of the second olefin monomer, including methyl acrylate, methyl methacrylate, butyl acrylate, butyl methacrylate, styrene, divinylbenzene, a-A One or several kinds of styrene. The amount of addition is preferably 2 to 18 parts, more preferably 3 to 12 parts. The addition of the olefin monomer can, on the one hand, increase the reaction efficiency of the polyfunctional group-containing monomer and, on the other hand, inhibit the degradation of the polyolefin. However, if the amount of the olefin monomer is more than 25 parts, the second olefin monomer will produce more homopolymer, which affects the performance of the coupled polyolefin.
( 4 ) 0.02〜10.0份 (重量份) 的引发剂, 包括过氧化二异丙苯、 过氧化 苯甲酰、 过氧化十二酰、 二叔丁基过氧化物、 叔丁基过氧化氢、 叔丁基过氧 化苯甲酸酯、 1, 4-双 (叔丁基过氧化异丙基) 苯等过氧化物引发剂以及偶氮
二异丁睛、 偶氮二异庚睛等的一种或者几种。 如果引发剂的用量低于 0.02份 (重量份) , 产生的自由基浓度太低, 会降低多官能团烯类单体与聚烯烃的 反应效率, 影响偶联聚烯烃的使用性能。但如果引发剂的用量大于 10.0份(重 量份) , 则会引起聚烯烃严重的交联和降解反应, 另外, 残存的引发剂还会 恶化偶联聚烯烃的性能。 (4) 0.02 to 10.0 parts by weight of an initiator, including dicumyl peroxide, benzoyl peroxide, dodecyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, Peroxide initiator such as t-butyl peroxybenzoate, 1, 4-bis(tert-butylperoxyisopropyl)benzene, and azo One or more of diisobutyl phthalate, azo diisoheptane, and the like. If the amount of the initiator is less than 0.02 part by weight, the concentration of the radical generated is too low, which lowers the reaction efficiency of the polyfunctional ethylenic monomer and the polyolefin, and affects the use properties of the coupled polyolefin. However, if the amount of the initiator is more than 10.0 parts by weight, serious crosslinking and degradation of the polyolefin may be caused, and in addition, the residual initiator may deteriorate the properties of the coupled polyolefin.
( 5 ) 聚烯烃的接枝反应可以通过溶液反应和熔融反应两种方法进行: 溶液反应是将除引发剂外的各种物料加入到二甲苯、 甲苯、 三氯苯、 氯 仿等有机溶剂中, 逐步升温至 100〜145度, 并搅拌, 形成 5%〜15%的均匀溶 液。 鼓氮气排除氧气后, 分 3〜5次逐步加入引发剂, 维持温度反应 2〜4小时。 反应结束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到接枝聚烯烃。 (5) The grafting reaction of the polyolefin can be carried out by a solution reaction and a melt reaction: the solution reaction is carried out by adding various materials other than the initiator to an organic solvent such as xylene, toluene, trichlorobenzene or chloroform. Gradually raise the temperature to 100 to 145 degrees and stir to form a uniform solution of 5% to 15%. After the nitrogen gas is removed from the drum, the initiator is gradually added in 3 to 5 times, and the temperature is maintained for 2 to 4 hours. After completion of the reaction, the reaction solution was cooled, and a solid precipitated, which was filtered and dried to obtain a graft polyolefin.
在溶液反应中, 如果反应温度低于 ioo°c, 聚烯烃可能溶解不完全, 使 接枝反应难以进行。 如果反应温度过高, 溶剂剧烈沸腾使接枝反应不能稳定 进行。 In the solution reaction, if the reaction temperature is lower than ioo °c, the polyolefin may be incompletely dissolved, making the grafting reaction difficult. If the reaction temperature is too high, the solvent is vigorously boiled so that the grafting reaction cannot be stably carried out.
熔融反应是将各种物料经高速混合后加入到哈克、 单螺杆挤出机、 双螺 杆挤出机、 密炼机、 班伯里混合机、 开炼机中, 于 130 °C〜250 °C范围内进行 熔融反应, 进一步优选为 120 °C〜200 °C范围内进行熔融反应, 反应时间为 lmin〜30min, 进一步优选为 3min〜8min。 将产物冷却、 切粒, 制得接枝聚 烯烃。 The melt reaction is carried out by mixing various materials at high speed and then adding them to a Huck, a single screw extruder, a twin screw extruder, an internal mixer, a Banbury mixer, and an open mill at 130 ° C to 250 °. The melting reaction is carried out in the range of C, and it is more preferable to carry out the melting reaction in the range of from 120 ° C to 200 ° C, and the reaction time is from 1 min to 30 min, more preferably from 3 min to 8 min. The product is cooled and pelletized to obtain a grafted polyolefin.
在熔融反应中, 如果反应温度低于 100 °C, 聚烯烃不能完全熔融, 接枝 反应难以进行。 如果反应温度高于 250 °C, 不但会降低聚烯烃的接枝率还会 使聚烯烃产物降解, 恶化其物理性能。 如果反应时间小于 lmin, 接枝反应不 能完全进行, 影响聚烯烃的接枝率, 残留的引发剂还会恶化聚烯烃产物的性 能。 如果反应时间大于 30min, 则有可能使聚烯烃降解。 In the melt reaction, if the reaction temperature is lower than 100 °C, the polyolefin cannot be completely melted, and the graft reaction is difficult to proceed. If the reaction temperature is higher than 250 °C, not only will the graft ratio of the polyolefin be lowered, but also the polyolefin product will be degraded and its physical properties deteriorated. If the reaction time is less than 1 min, the grafting reaction does not proceed completely, affecting the graft ratio of the polyolefin, and the residual initiator may deteriorate the properties of the polyolefin product. If the reaction time is more than 30 minutes, it is possible to degrade the polyolefin.
( 6 ) 100份 (重量份) 的接枝聚烯烃树脂, 它是通过上述的聚烯烃接枝 方法制备的。 (6) 100 parts by weight of a graft polyolefin resin which is produced by the above-described polyolefin grafting method.
( 7 ) 0. 1〜20份 (重量份) 含多官能团的有机偶联剂, 结构式如式 I:
、 、F 式 I (7) 0. 1~20 parts by weight of a polyfunctional organic coupling agent having the formula: , , F Formula I
R, 代表多官能团偶联剂的主要结构, 如烷基、 芳基、 芳烷基、 齐聚物 或者含有各种杂原子的有机结构。 对于溶液反应, 优选使用 R为烷基的有机 物; 对于熔融共混反应优选 R为齐聚物或者芳烷基的有机物, 这样可以增强 含多官能团有机偶联剂与接枝聚烯烃的相容性, 使偶联反应顺利进行。 R, represents the main structure of the polyfunctional coupling agent, such as an alkyl group, an aryl group, an aralkyl group, an oligomer or an organic structure containing various hetero atoms. For the solution reaction, it is preferred to use an organic substance in which R is an alkyl group; for the melt blending reaction, it is preferred that R is an oligomer or an aralkyl organic substance, which can enhance the compatibility of the polyfunctional organic coupling agent with the grafted polyolefin. , the coupling reaction proceeds smoothly.
F, 代表各种功能性官能团, 如羧基、 伯胺基、 仲胺基、 羟基、 环氧基、 异氰酸酯基、 酰胺基、 磺酸基、 酰氯基等, 优选使用 F为伯胺基、 羧基的官 能团, 进一步优选使用 F为伯胺基的官能团, 这样可以加快含多官能团有机 物与接枝聚烯烃的反应速度。 F, representing various functional functional groups, such as a carboxyl group, a primary amino group, a secondary amino group, a hydroxyl group, an epoxy group, an isocyanate group, an amide group, a sulfonic acid group, an acid chloride group, etc., preferably using F as a primary amino group or a carboxyl group. As the functional group, it is further preferred to use a functional group in which F is a primary amino group, which accelerates the reaction rate of the polyfunctional organic group with the grafted polyolefin.
n , 代表官能团的个数, n l, 优选 n = 2, 此时可以有效控制聚烯烃的 偶联度, 如果 n太小, 可能不能产生偶联反应, 如果 n太大, 会使偶联反应失 去控制, 恶化偶联聚烯烃的性能。 n , represents the number of functional groups, nl, preferably n = 2, at this time can effectively control the degree of coupling of the polyolefin, if n is too small, may not produce a coupling reaction, if n is too large, the coupling reaction will be lost Control, deteriorate the properties of the coupled polyolefin.
( 8 ) 0〜10份 (重量份) 的抗氧剂含量, 包括 2, 6-二叔丁基 -4-乙基苯 酚、 2, 6-二叔丁基 -4-甲基苯酚、 2, 6-二叔丁基 - α -二甲氨基-对甲酚、 2, 4, 6-三叔丁基苯酚、 硫代二丙酸二月桂酯、 硫代二丙酸二 (十八酯) 、 硫代二 丙酸二 (十四酯) 、 抗氧剂 1010、 抗氧剂 CA、 抗氧剂 B215以及抗氧剂 B225 中的一种或几种。 抗氧剂的加入可以调节偶联聚烯烃的反应情况和熔体流动 性, 但是如果加入量大于 10份, 会恶化偶联聚烯烃的使用性能。 (8) 0 to 10 parts by weight of the antioxidant content, including 2,6-di-tert-butyl-4-ethylphenol, 2,6-di-tert-butyl-4-methylphenol, 2, 6-di-tert-butyl-α-dimethylamino-p-cresol, 2,4,6-tri-tert-butylphenol, dilauryl thiodipropionate, di(octadecyl) thiodipropionate, One or more of di(tetradecyl thiodipropionate), antioxidant 1010, antioxidant CA, antioxidant B215, and antioxidant B225. The addition of the antioxidant can adjust the reaction state and melt flowability of the coupled polyolefin, but if it is added in an amount of more than 10 parts, the use properties of the coupled polyolefin are deteriorated.
( 9 ) 通常可以采用以下两种方法进行接枝聚烯烃的偶联, 从而获得本 发明的偶联聚烯烃。 (9) The coupling of the grafted polyolefin can be generally carried out by the following two methods, thereby obtaining the coupled polyolefin of the present invention.
1 ) 溶液反应法: 按照上文说明的配料, 将按照上述方法制备的接枝聚 烯烃加入到二甲苯、 甲苯、 三氯苯、 氯仿等有机溶剂中, 逐步升温, 并搅拌, 形成 5%〜15%的均匀溶液。 鼓氮排除氧气后, 将含多官能团的有机物一次性 加入到溶液中, 维持温度反应 0.5〜1小时。 反应结束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到偶联聚烯烃。 1) Solution reaction method: According to the above-mentioned ingredients, the grafted polyolefin prepared according to the above method is added to an organic solvent such as xylene, toluene, trichlorobenzene, chloroform, etc., and gradually heated, and stirred to form 5%~ 15% homogeneous solution. After the nitrogen is removed from the drum, the polyfunctional organic substance is added to the solution at a time, and the temperature is maintained for 0.5 to 1 hour. After completion of the reaction, the reaction solution was cooled, and a solid precipitated, which was filtered and dried to obtain a coupled polyolefin.
2 ) 熔融反应法: 按照上文说明的配料, 将按照上述方法制备的接枝聚
烯烃、 抗氧剂与含多官能团的有机物经高速混合后逐步加入到哈克、 单螺杆 挤出机、 双螺杆挤出机、 密炼机、 班伯里混合机、 开炼机中, 于 160°C〜190 °C下熔融反应, 时间为 lmin〜30min, 经切粒或粉碎后造粒, 即得到偶联聚 烯烃。 2) Melt reaction method: According to the ingredients described above, the graft polymerization prepared according to the above method The olefin, antioxidant and polyfunctional organic matter are mixed at high speed and then gradually added to the Huck, single screw extruder, twin screw extruder, internal mixer, Banbury mixer, open mill, at 160 The reaction is melted at a temperature of from ° C to 190 ° C for a period of from 1 min to 30 min. After granulation or pulverization, granulation is carried out to obtain a coupled polyolefin.
实施例与对照例: Examples and comparisons:
实施例与对照例 1〜2是在溶液中进行长枝化聚丙烯的制备: Examples and Comparative Examples 1 to 2 are preparations of long-branched polypropylene in solution:
实施例 1 : 取聚丙烯 EPS30R (齐鲁石化股份有限公司) 100克, 1010抗氧 剂 0.1克, 加入到 2000ml的烧瓶中, 然后加入 1300克二甲苯, 逐步升温至 140 °C。 待固体全部溶解后, 加入丙烯酸接枝单体 2克, 苯乙烯 2克, 然后将 0.36 克过氧化苯甲酰在 30分钟内分 5次加入到烧瓶中, 维持 140°C反应。 反应结束 后, 将烧瓶冷却至室温, 加入 100克丙酮, 经搅拌待固体完全析出后, 放在 真空烘箱中干燥, 得到接枝聚烯烃。 丙烯酸与聚丙烯的接枝率结果见表 1。 Example 1: Polypropylene EPS30R (Qilu Petrochemical Co., Ltd.) 100 g, 1010 antioxidant 0.1 g, was added to a 2000 ml flask, and then 1300 g of xylene was added thereto, and the temperature was gradually raised to 140 °C. After the solid was completely dissolved, 2 g of an acrylic graft monomer, 2 g of styrene was added, and then 0.36 g of benzoyl peroxide was added to the flask 5 times in 30 minutes to maintain the reaction at 140 °C. After completion of the reaction, the flask was cooled to room temperature, 100 g of acetone was added, and the solid was completely precipitated by stirring, and then dried in a vacuum oven to obtain a graft polyolefin. The grafting ratio results of acrylic acid and polypropylene are shown in Table 1.
取 50g通过上述方法制备的接枝聚丙烯, 1010抗氧剂 0.05克加入到 2000ml 的烧瓶中, 然后加入 1000克二甲苯, 逐步升温至 140°C。 待固体全部溶解后, 将 1.4克 1, 4丁二醇二缩水甘油醚作为多官能团偶联剂在 30分钟内分 5次加入 到烧瓶中, 维持 140°C反应。 反应结束后, 将烧瓶冷却至室温, 加入 100克丙 酮, 经搅拌待固体完全析出后, 放在真空烘箱中干燥, 得到长枝化聚烯烃。 长枝化聚烯烃的各项性能列于表 1中。 50 g of the grafted polypropylene prepared by the above method, 0.05 g of 1010 antioxidant was added to a 2000 ml flask, and then 1000 g of xylene was added thereto, and the temperature was gradually raised to 140 °C. After all the solids were dissolved, 1.4 g of 1,4 butanediol diglycidyl ether was added as a polyfunctional coupling agent to the flask in 5 minutes over 30 minutes, and the reaction was maintained at 140 °C. After completion of the reaction, the flask was cooled to room temperature, 100 g of acetone was added, and the solid was completely precipitated by stirring, and then dried in a vacuum oven to obtain a long-branched polyolefin. The properties of the long-branched polyolefin are listed in Table 1.
对照例 1 : 取 50g实施例 1制备的接枝聚丙烯。 接枝聚丙烯的偶联方法与 实施例 1相同, 只是将 1.2克乙二醇二缩水甘油醚作为偶联剂加入到接枝聚丙 烯溶液中进行偶联反应。 得到的长枝化聚丙烯的各项性能列于表 1中。 Comparative Example 1: 50 g of the grafted polypropylene prepared in Example 1 was taken. The grafting method of the grafted polypropylene was the same as in Example 1, except that 1.2 g of ethylene glycol diglycidyl ether was added as a coupling agent to the grafted polypropylene solution for coupling reaction. The properties of the obtained long-branched polypropylene are shown in Table 1.
实施例 2 : 它的聚丙烯接枝方法与实施例 1相同, 只是将甲基丙烯酸羟乙 酯作为接枝单体与聚丙烯进行接枝反应。 它的偶联方法也与实施例 1相同, 只是将 0.65克六亚甲基二异氰酸酯 (HDI ) 作为偶联剂加入到接枝聚丙烯溶 液中进行偶联反应。 甲基丙烯酸羟乙酯与聚丙烯的接枝率结果以及得到的长 枝化聚烯烃的各项性能列于表 1中。 Example 2: The polypropylene grafting method was the same as in Example 1, except that glycolic acid methacrylate was grafted with polypropylene as a grafting monomer. The coupling method was also the same as in Example 1, except that 0.65 g of hexamethylene diisocyanate (HDI) was added as a coupling agent to the grafted polypropylene solution for the coupling reaction. The results of the graft ratio of hydroxyethyl methacrylate to polypropylene and the properties of the obtained long-branched polyolefin are shown in Table 1.
对照例 2 : 取 50g实施例 2制备的接枝聚丙烯。 接枝聚丙烯的偶联方法与 实施例 1相同, 只是将 0.67克甲苯 -2, 4-二异氰酸酯 (TDI ) 作为偶联剂加入 到接枝聚丙烯溶液中进行偶联反应。 得到的长枝化聚丙烯的各项性能列于表
1中。 Comparative Example 2: 50 g of the grafted polypropylene prepared in Example 2 was taken. The coupling method of the grafted polypropylene was the same as in Example 1, except that 0.67 g of toluene-2,4-diisocyanate (TDI) was added as a coupling agent to the grafted polypropylene solution for coupling reaction. The properties of the obtained long-branched polypropylene are listed in the table. 1 in.
实施例与对照例 3〜4是采用熔融法进行长枝化聚丙烯的制备: Examples and Comparative Examples 3 to 4 are preparations of long-branched polypropylene by a melt method:
实施例 3 : 取聚丙烯 EPS30R (齐鲁石化股份有限公司) 10公斤, GMA接 枝单体 0.2公斤, 苯乙烯 0.2公斤, 过氧化二异丙苯 36克, 将过氧化二异丙苯 溶解于 GMA和苯乙烯的单体中, 然后全部放入高速混合机中混合 2分钟, 出 料。 将混合料加入到已经预热到 170 °C的双螺杆挤出机中, 以 50rpm的转速反 应挤出。 挤出产物经切粒后得到接枝聚烯烃。 GMA与聚烯烃的接枝率结果见 表 1。 Example 3: Take polypropylene EPS30R (Qilu Petrochemical Co., Ltd.) 10 kg, GMA graft monomer 0.2 kg, styrene 0.2 kg, dicumyl peroxide 36 g, dissolve dicumyl peroxide in GMA And styrene monomer, and then all mixed in a high-speed mixer for 2 minutes, discharging. The mixture was added to a twin-screw extruder which had been preheated to 170 ° C, and the reaction was extruded at 50 rpm. The extruded product is pelletized to obtain a grafted polyolefin. The grafting ratio results of GMA and polyolefin are shown in Table 1.
取 5公斤通过上述方法制备的接枝聚丙烯, 抗氧剂 20克, 己二胺 40.8克, 然后全部放入高速混合机中混合 2分钟, 出料。 将混合料加入到到已经预热 到 180 °C的双螺杆挤出机中, 以 80rpm的转速反应挤出。 挤出产物经切粒后得 到偶联聚烯烃。 长枝化聚烯烃的各项性能列于表 2中。 5 kg of grafted polypropylene prepared by the above method, 20 g of an antioxidant, 40.8 g of hexamethylenediamine, and then all mixed in a high-speed mixer for 2 minutes were discharged. The mixture was added to a twin-screw extruder which had been preheated to 180 ° C and reacted and extruded at 80 rpm. The extruded product is pelletized to obtain a coupled polyolefin. The properties of the long-branched polyolefin are listed in Table 2.
对照例 3 : 取 5公斤实施例 3制备的接枝聚丙烯。 接枝聚丙烯的偶联方法 与实施例 3相同,只是将 3 1.0克丁二胺作为偶联剂加入到接枝聚丙烯中进行偶 联反应。 得到的长枝化聚丙烯的各项性能列于表 2中。 Comparative Example 3: 5 kg of the grafted polypropylene prepared in Example 3 was taken. The coupling method of the grafted polypropylene was the same as in Example 3 except that 3 1.0 g of butanediamine was added as a coupling agent to the grafted polypropylene for the coupling reaction. The properties of the obtained long-branched polypropylene are shown in Table 2.
实施例 4 : 它的聚丙烯接枝方法与实施例 3相同, 只是将马来酸酐作为接 枝单体与聚丙烯进行接枝反应。 它的偶联方法也与实施例 3相同, 只是将 74.5 克辛二醇作为偶联剂加入到接枝聚丙烯中进行偶联反应。 马来酸酐与聚丙烯 的接枝率结果以及得到的长枝化聚烯烃的各项性能列于表 2中。 Example 4: Its polypropylene grafting method was the same as in Example 3 except that maleic anhydride was grafted with polypropylene as a grafting monomer. The coupling method was also the same as in Example 3 except that 74.5 g of octanediol was added as a coupling agent to the grafted polypropylene for coupling reaction. The results of the graft ratio of maleic anhydride to polypropylene and the properties of the obtained long-branched polyolefin are shown in Table 2.
对照例 4 : 取 5公斤实施例 4制备的接枝聚丙烯。 接枝聚丙烯的偶联方法 与实施例 4相同,只是将 32.7克乙二醇作为偶联剂加入到接枝聚丙烯中进行偶 联反应。 得到的长枝化聚丙烯的各项性能列于表 2中。
Comparative Example 4: 5 kg of the grafted polypropylene prepared in Example 4 was taken. The coupling method of the grafted polypropylene was the same as in Example 4 except that 32.7 g of ethylene glycol was added as a coupling agent to the grafted polypropylene for the coupling reaction. The properties of the obtained long-branched polypropylene are shown in Table 2.
表 1 Table 1
从表 1中可以看出, 用丙烯酸和甲基丙烯酸羟乙酯都可以与聚丙烯发生 接枝反应, 并且接枝率都比较高, 而且甲基丙烯酸羟乙酯比丙烯酸的接枝率 要高, 这可能是甲基丙烯酸羟乙酯与聚丙烯的相容性比丙烯酸更好的缘故。 It can be seen from Table 1 that both acrylic acid and hydroxyethyl methacrylate can be grafted with polypropylene, and the graft ratio is relatively high, and the graft ratio of hydroxyethyl methacrylate to acrylic acid is higher. This may be because hydroxyethyl methacrylate is more compatible with polypropylene than acrylic acid.
用 1, 4丁二醇二缩水甘油醚和 HDI进行偶联的长枝化聚丙烯的熔体流动 速率低于 EPS30R,储能模量高于 EPS30R, 说明经过这两种偶联剂偶联后的聚 丙烯得到了有效枝化。 而用乙二醇二缩水甘油醚和 TDI偶联后的聚丙烯的性 能被恶化。 这是因为后两种偶联剂的分子链比较短, 在偶联反应时被聚丙烯 分子链包埋, 导致偶联反应不能进行。 而较长的偶联剂可以在不同的聚丙烯 分子链之间进行偶联反应, 使聚丙烯产生枝化。
表 2 The long-branched polypropylene coupled with 1,4 butanediol diglycidyl ether and HDI has a lower melt flow rate than EPS30R, and the storage modulus is higher than EPS30R, indicating that after the coupling of the two coupling agents The polypropylene is effectively branched. The performance of polypropylene coupled with ethylene glycol diglycidyl ether and TDI was deteriorated. This is because the latter two coupling agents have a relatively short molecular chain and are embedded in the molecular chain of the polypropylene during the coupling reaction, resulting in a failure of the coupling reaction. The longer coupling agent can carry out the coupling reaction between different polypropylene molecular chains to cause the polypropylene to be branched. Table 2
从表 2 同样可以看出, GMA和马来酸酐与聚丙烯有很好的接枝效果, 两 者的接枝效率达到了 80 %。而且具有长链结构的己二胺和辛二醇能够使接枝 聚丙烯产生良好的偶联效果。
It can also be seen from Table 2 that GMA and maleic anhydride have good grafting effect with polypropylene, and the grafting efficiency of the two reaches 80%. Moreover, hexamethylenediamine and octanediol having a long-chain structure can produce a good coupling effect for the grafted polypropylene.
Claims
1. 一种聚烯烃分子链的偶联方法, 其特征在于, 该方法通过溶液接枝反 应或者熔融接枝反应, 在 0.02〜10.0重量份引发剂的作用下, 使 0〜15重量份 含多官能团的烯类单体在 0〜 15重量份第二烯烃单体协同作用下与 100重量 份聚烯烃在一定温度下进行接枝反应, 制备侧链带有官能团的接枝聚烯烃; 取 100重量份的接枝聚烯烃, 通过溶液反应或者熔融共混反应, 在一定温度 下加入 0. 1〜20重量份的多官能团有机偶联剂和 0〜 10.0重量份的抗氧剂将所 述接枝聚烯烃进行偶联。 A method for coupling a molecular chain of a polyolefin, characterized in that the method comprises a solution grafting reaction or a melt grafting reaction, and comprises 0 to 15 parts by weight under the action of 0.02 to 10.0 parts by weight of an initiator. The functional group of the ethylenic monomer is grafted with 100 parts by weight of the polyolefin at a certain temperature under the synergistic action of 0 to 15 parts by weight of the second olefin monomer to prepare a grafted polyolefin having a functional group in the side chain; a grafted polyolefin, by solution reaction or melt blending reaction, adding 0.1 to 20 parts by weight of a polyfunctional organic coupling agent and 0 to 10.0 parts by weight of an antioxidant at a certain temperature to graft the graft The polyolefin is coupled.
2. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的聚烯烃包括通用聚丙烯、 通用聚乙烯或乙烯丙烯的共聚物, 其熔体流 动速率为 0. 1g/10min〜50 g/10min ; 所述的含多官能团的烯类单体包括丙烯 酸、 马来酸酐、 甲基丙烯酸、 富马酸、 衣康酸、 十一碳烯酸、 甲基丙烯酸缩 水甘油酯、 丙烯酰胺、 N-羟甲基丙烯酰胺、 丙烯酸羟乙酯、 丙烯酸羟丙酯中 的一种或者几种; 所述的第二烯烃单体包括苯乙烯、 二乙烯基苯、 a -甲基苯 乙烯、 丙烯酸甲酯、 甲基丙烯酸甲酯、 丙烯酸丁酯、 甲基丙烯酸丁酯中的一 种或几种; 所述的引发剂包括过氧化二异丙苯、 过氧化苯甲酰、 过氧化十二 酰、 二叔丁基过氧化物、 叔丁基过氧化氢、 叔丁基过氧化苯甲酸酯、 1, 4- 双 (叔丁基过氧化异丙基) 苯, 或者偶氮二异丁睛、 偶氮二异庚睛中的一种 或者几种。 2 . The method for coupling a polyolefin molecular chain according to claim 1 , wherein the polyolefin comprises a copolymer of general-purpose polypropylene, general-purpose polyethylene or ethylene propylene, and the melt flow rate thereof is 0. 1g/10min~50 g/10min ; the polyfunctional group-containing monomer includes acrylic acid, maleic anhydride, methacrylic acid, fumaric acid, itaconic acid, undecylenic acid, methacrylic acid One or more of glycidyl ester, acrylamide, N-methylol acrylamide, hydroxyethyl acrylate, hydroxypropyl acrylate; the second olefin monomer comprises styrene, divinylbenzene, a One or more of methyl styrene, methyl acrylate, methyl methacrylate, butyl acrylate, butyl methacrylate; the initiator includes dicumyl peroxide, benzoyl peroxide Acyl, dodecyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, t-butyl peroxybenzoate, 1, 4-bis(tert-butylperoxyisopropyl)benzene, Or one of azobisisobutanide and azobishesin Or several.
3. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的溶液接枝法包括如下步骤: 将 100重量份的聚烯烃树脂、 0〜15重量份 的含多官能团的烯类单体和 0〜 15重量份的第二烯烃单体加入到有机溶剂 中, 逐步升温, 并搅拌, 形成 5%〜15%的均匀溶液, 鼓氮气排除氧气后, 分 3〜5次逐步加入 0.02〜10.0重量份引发剂, 维持温度反应 2〜4小时, 反应结 束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到接枝聚烯烃。 The method for coupling a polyolefin molecular chain according to claim 1, wherein the solution grafting method comprises the following steps: 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight The polyfunctional group-containing monomer and 0 to 15 parts by weight of the second olefin monomer are added to the organic solvent, gradually heated, and stirred to form a uniform solution of 5% to 15%, and after the nitrogen gas is removed by the nitrogen gas, the fraction is 3 5% to 50.0 parts by weight of the initiator was gradually added thereto, and the temperature was maintained for 2 to 4 hours. After the completion of the reaction, the reaction solution was cooled, and the solid was precipitated. After filtration and drying, a graft polyolefin was obtained.
4. 根据权利要求 3所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的有机溶剂包括二甲苯、 甲苯、 三氯苯、 氯仿。 The method for coupling a polyolefin molecular chain according to claim 3, wherein the organic solvent comprises xylene, toluene, trichlorobenzene, chloroform.
5. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于,
所述的熔融接枝法包括如下步骤: 将 100重量份的聚烯烃树脂、 0〜15重量份 的含多官能团的烯类单体、 0〜15重量份的第二烯烃单体和 0.02〜10.0重量份 引发剂经高速混合后加入到哈克、 单螺杆挤出机、 双螺杆挤出机、 密炼机、 班伯里混合机或开炼机中, 于 130 °C〜250 °C下进行熔融接枝反应, 反应 lmin〜30min, 将产物冷却、 切粒, 制得接枝聚烯烃。 5. The method for coupling a polyolefin molecular chain according to claim 1, wherein: The melt grafting method comprises the steps of: 100 parts by weight of a polyolefin resin, 0 to 15 parts by weight of a polyfunctional group-containing monomer, 0 to 15 parts by weight of a second olefin monomer, and 0.02 to 10.0 The parts by weight of the initiator are mixed at high speed and then added to a Huck, single screw extruder, twin screw extruder, internal mixer, Banbury mixer or open mill at 130 ° C to 250 ° C. The melt grafting reaction is carried out for 1 min to 30 min, and the product is cooled and pelletized to obtain a graft polyolefin.
6. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的多官能团有机偶联剂的结构式如式 I: The method for coupling a polyolefin molecular chain according to claim 1, wherein the polyfunctional organic coupling agent has the structural formula:
式 IFormula I
R, 代表多官能团偶联剂的主要结构, 包括烷基、 芳基、 芳烷基、 齐聚 物或者含有各种杂原子的有机结构; R, representing the main structure of the polyfunctional coupling agent, including an alkyl group, an aryl group, an aralkyl group, an oligomer or an organic structure containing various hetero atoms;
F, 代表各种功能性官能团, 包括羧基、 伯胺基、 仲胺基、 羟基、 环氧 基、 异氰酸酯基、 酰胺基、 磺酸基、 酰氯基; F, representing various functional functional groups, including a carboxyl group, a primary amino group, a secondary amino group, a hydroxyl group, an epoxy group, an isocyanate group, an amide group, a sulfonic acid group, an acid chloride group;
n , 代表官能团的个数, n l。 n , represents the number of functional groups, n l.
7. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的抗氧剂包括 2, 6-二叔丁基 -4-乙基苯酚、 2, 6-二叔丁基 -4-甲基苯酚、 2, 6-二叔丁基 - a -二甲氨基-对甲酚、 2, 4, 6-三叔丁基苯酚、 硫代二丙酸二 月桂酯、 硫代二丙酸二 (十八酯) 、 硫代二丙酸二 (十四酯) 、 抗氧剂 1010、 抗氧剂 CA、 抗氧剂 B215以及抗氧剂 B225中的一种或几种。 The method for coupling a polyolefin molecular chain according to claim 1, wherein the antioxidant comprises 2,6-di-tert-butyl-4-ethylphenol, 2,6- Di-tert-butyl-4-methylphenol, 2,6-di-tert-butyl-a-dimethylamino-p-cresol, 2,4,6-tri-tert-butylphenol, dilauryl thiodipropionate One or more of bis(octadecyl thiodipropionate), di(tetradecyl thiodipropionate), antioxidant 1010, antioxidant CA, antioxidant B215, and antioxidant B225 Kind.
8. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的溶液接枝法包括如下步骤: 将制备的接枝聚烯烃和抗氧剂加入到聚烯 烃溶剂中, 逐步升温, 并搅拌, 形成 5%〜15%的均匀溶液, 鼓氮气排除氧气 后, 一次性加入含多官能团的有机偶联剂, 维持温度反应 0.1〜1小时, 反应 结束后, 将反应溶液降温, 固体析出, 经过滤、 干燥后得到偶联聚烯烃。 The method for coupling a polyolefin molecular chain according to claim 1, wherein the solution grafting method comprises the following steps: adding the prepared graft polyolefin and an antioxidant to the polyolefin In the solvent, gradually increase the temperature, and stir to form a uniform solution of 5%~15%. After removing the oxygen by the nitrogen gas, the organic coupling agent containing the polyfunctional group is added in one time, and the temperature reaction is maintained for 0.1 to 1 hour. After the reaction is finished, The reaction solution was cooled, and a solid precipitated, which was filtered and dried to obtain a coupled polyolefin.
9. 根据权利要求 8所述的一种聚烯烃分子链的偶联方法, 其特征在于, 所述的聚烯烃溶剂包括二甲苯、 甲苯、 三氯苯、 氯仿。 The method for coupling a polyolefin molecular chain according to claim 8, wherein the polyolefin solvent comprises xylene, toluene, trichlorobenzene, chloroform.
10. 根据权利要求 1所述的一种聚烯烃分子链的偶联方法,其特征在于,
所述的熔融接枝法包括如下步骤: 将接枝聚烯烃、 抗氧剂和含多官能团的有 机偶联剂在高混机中混合均匀, 然后加入到哈克、 单螺杆挤出机、 双螺杆挤 出机、密炼机、班伯里混合机或开炼机中, 于 130 °C〜250 °C下进行熔融反应, 反应 lmin〜30min, 将产物冷却、 切粒, 制得偶联聚烯烃。
10. The method for coupling a polyolefin molecular chain according to claim 1, wherein: The melt grafting method comprises the following steps: mixing the grafted polyolefin, the antioxidant and the polyfunctional organic coupling agent in a high mixer, and then adding to the Huck, single screw extruder, double In a screw extruder, an internal mixer, a Banbury mixer or an open mill, the melting reaction is carried out at 130 ° C to 250 ° C for 1 min to 30 min, and the product is cooled and pelletized to obtain a coupled polymer. Olefins.
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