阅读说明：本技术 (α-二亚胺)镍络合物组合物及其应用 ((alpha-diimine) nickel complex compositions and uses thereof ) 是由 傅智盛 于 2021-06-23 设计创作，主要内容包括：本发明涉及烯烃催化聚合技术,旨在提供一种(α-二亚胺)镍络合物组合物及其应用。该组合物用于催化乙烯聚合,是由(α-二亚胺)镍络合物A、B、C中的两种或两种以上组成。用(α-二亚胺)镍络合物组合物催化乙烯聚合,可以原位生成不同链结构的聚乙烯混合物,不同的组分发挥各自的特性,从而赋予聚合产物优异的综合性能。这个通过物理共混的方法是不容易实现的,尤其是将难熔难溶的超高分子量聚乙烯添加到其它聚合物中,用物理共混的方法更是难上加难。因此,用(α-二亚胺)镍络合物组合物催化乙烯聚合,通过原位共混的方法,制备综合性能优异的聚乙烯,具有生产工艺简单,生产成本低,生产效率高,易于工业化的优点。(The invention relates to an olefin catalytic polymerization technology, and aims to provide an (alpha-diimine) nickel complex composition and application thereof. The composition is used for catalyzing ethylene polymerization and consists of two or more than two of (alpha-diimine) nickel complexes A, B, C. The (alpha-diimine) nickel complex composition is used for catalyzing ethylene polymerization, polyethylene mixtures with different chain structures can be generated in situ, and different components exert respective characteristics, so that excellent comprehensive performance is endowed to a polymerization product. This method of physical blending is not easy to achieve, especially the addition of refractory, poorly soluble ultra high molecular weight polyethylene to other polymers is more difficult to achieve by physical blending. Therefore, the (alpha-diimine) nickel complex composition is used for catalyzing ethylene polymerization, and the polyethylene with excellent comprehensive performance is prepared by an in-situ blending method, and has the advantages of simple production process, low production cost, high production efficiency and easiness in industrialization.)

1. An (alpha-diimine) nickel complex composition for catalyzing the polymerization of ethylene, the composition comprising two or more of (alpha-diimine) nickel complexes A, B, C; wherein the content of the first and second substances,

the molecular structural formula of the (alpha-diimine) nickel complex A is shown as follows:

the molecular structural formula of the (alpha-diimine) nickel complex B is as follows:

the molecular structural formula of the (alpha-diimine) nickel complex C is as follows:

2. the (α -diimine) nickel complex composition of claim 1, wherein the (α -diimine) nickel complex a is used to catalyze the formation of polyethylene having a degree of branching of not less than 60 branches/1000 carbons and a weight average molecular weight of not more than 420 kg/mole; the (alpha-diimine) nickel complex B is used for catalyzing ethylene polymerization to generate polyethylene with the weight average molecular weight of 700-10000 kg/mol and the branching degree of 60-125 branched chains/1000 carbons; the (alpha-diimine) nickel complex C is used for catalyzing ethylene polymerization to generate polyethylene with the weight average molecular weight of 20-10000 kg/mol and the branching degree of 0-60 branched chains/1000 carbons.

3. The (α -diimine) nickel complex composition of claim 1, wherein the (α -diimine) nickel complex a is prepared as follows:

the preparation method comprises the following specific steps:

(1) under the protection of nitrogen, carrying out dehydration condensation reaction of amino and carbonyl on 2 equivalents of aniline and 1 equivalent of methylglyoxal, monitoring the reaction end point by using thin-layer chromatography, stopping stirring after the reaction is completed, and vacuumizing to remove the solvent; separating and purifying by column chromatography to obtain alpha-diimine;

(2) under the anhydrous and oxygen-free conditions, complexing alpha-diimine with any one of ethylene glycol dimethyl ether nickel dibromide, ethylene glycol dimethyl ether nickel dichloride, nickel chloride tetrahydrate or nickel chloride hexahydrate to obtain the (alpha-diimine) nickel complex A.

4. The (α -diimine) nickel complex composition of claim 1, wherein: the preparation process of the (alpha-diimine) nickel complex B is as follows:

the preparation method comprises the following specific steps:

(1) weighing ethylene substituted acenaphthenequinone 1,2, 6-di (diphenylmethyl) -4-methylaniline and ZnCl₂Putting into a flask, adding glacial acetic acid, fully stirring, heating to 120 ℃, and carrying out reflux reaction for 2 hours; after the reaction is finished, mixingCooling the product to room temperature, filtering and separating to obtain a solid, washing, and adding dichloromethane to completely dissolve the solid; adding potassium oxalate solution and stirring vigorously for 30 minutes to generate zinc oxalate precipitate in a water phase; standing, taking an upper organic layer, washing with deionized water, evaporating to dryness, and then drying in vacuum to obtain solid powder which is a compound 2;

the molar ratio of the used amount of each raw material is as follows: ethylene substituted acenaphthenequinonediquinone 1: 2, 6-bis (diphenylmethyl) -4-methylaniline: ZnCl₂＝0.8∶1∶1；

(2) Taking compound 2 and ZnCl₂Putting into a flask, adding glacial acetic acid, fully stirring, and heating to 120 ℃; injecting 2, 6-diisopropylaniline, carrying out reflux reaction for 30 minutes, cooling to room temperature, filtering and separating to obtain a solid, washing, and adding dichloromethane to completely dissolve the solid; adding potassium oxalate solution and stirring vigorously for 30 minutes to generate zinc oxalate precipitate in a water phase; standing, collecting the upper organic layer, washing with deionized water, and adding anhydrous MgSO₄The powder was stirred overnight to remove residual moisture; filtering, evaporating the solvent to dryness, adding n-hexane for washing, and performing vacuum drying to obtain a solid powdery compound 3;

the molar ratio of the used amount of each raw material is as follows: compound 2: ZnCl₂2, 6-diisopropylaniline is 0.52: 0.7: 1;

(3) reacting (DME) NiBr₂Adding the compound 3 and dichloromethane into a sealed reaction bottle protected by nitrogen, and stirring and reacting for 24 hours at room temperature; pumping out dichloromethane, collecting the dichloromethane by using a cold trap, washing the dichloromethane by using ether, and pumping out the dichloromethane to obtain orange solid powder, namely the (alpha-diimine) nickel complex B;

the molar ratio of the used amount of each raw material is as follows: (DME) NiBr₂Compound 3 is 0.12: 0.125.

5. The (α -diimine) nickel complex composition of claim 1, wherein: each (alpha-diimine) nickel complex is combined in pairs or three of the following ways:

when the complex A and the complex B are combined, the molar ratio of the complex A to the complex B is 99: 1-50: 50;

when the complex A and the complex C are combined, the molar ratio of the complex A to the complex C is 99: 1-50: 50;

when the complex B and the complex C are combined, the molar ratio of the complex B to the complex C is 99: 1-1: 99;

when the three are used simultaneously, the molar ratio of the complex A to the complex B to the complex C is 100 (1-100) to 1-100.

6. The method of using the (α -diimine) nickel complex composition of claim 1, wherein: the novel polyethylene material (NPE) is prepared by catalyzing ethylene polymerization by using the (alpha-diimine) nickel complex composition as a catalyst.

7. The method of application of claim 6, wherein: in the process of catalyzing ethylene polymerization, a cocatalyst is used, and the cocatalyst is a composition of alkyl metal and borate; wherein the content of the first and second substances,

the alkyl metal is one or more of trimethylaluminum, triisobutylaluminum, triethylaluminum, diethyl aluminum monochloride, ethyl aluminum dichloride, ethyl aluminum sesquichloride and diethyl zinc;

the borate is sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate, N-dimethylanilinium tetrakis (pentafluorophenyl) borate or triphenylmethyl tetrakis (pentafluorophenyl) borate;

the molar ratio of the alkylaluminum borate to the diethyl zinc (α -diimine) nickel complex is 50 to 500:2 to 0.5:0 to 100: 1.

8. Use of the novel polyethylene material (NPE) prepared by the process of claim 6, or of a composition comprising the novel polyethylene material (NPE), as, or in the manufacture of, any of: solar photovoltaic cell packaging adhesive films, conveyor belt cover stock, tire tread stock and films, at least one layer of a multilayer film, at least one layer of a laminate, a foamed article, a polypropylene impact modifier, a fiber, a nonwoven fabric, an injection molded article, a blow molded article, a rotational molded article, or an adhesive.

Technical Field

The invention relates to the field of olefin catalytic polymerization, in particular to an (alpha-diimine) nickel complex composition and application thereof in catalyzing ethylene polymerization to prepare a novel polyethylene material with excellent comprehensive performance.

Background

Polyolefin is a basic material related to the national civilization, and is widely applied to various fields of industry, agriculture, national defense and the like due to the excellent performance, various varieties, easily available raw materials, low price and the like. The development and application of new catalyst systems are one of the core drivers for the advancement and development of the polyolefin industry, and are the key to controlling the structure, composition and performance of polyolefins.

Because of its special ability to "chain walk", the (alpha-diimine) nickel olefin catalyst can catalyze ethylene polymerization to obtain a series of polyethylenes with linear to high branching degree. The electronegativity of the active center and the steric hindrance around the active center are adjusted by changing the size of a substituent group and the electron pulling/donating performance of a catalyst ligand, so that the chain transfer reaction in the polymerization process is controlled, and the polyethylene with the molecular weight of thousands to tens of millions can be prepared. Therefore, the (alpha-diimine) nickel olefin catalyst can catalyze ethylene polymerization to obtain polyethylene with different branching degrees, different molecular weights and different properties.

The properties of polyethylene are closely related to its chain structure, including degree of branching and molecular weight. Polyethylene with low branching degree is easy to crystallize, has high mechanical strength but poor rebound resilience, and can only be used as plastics; the polyethylene with high branching degree is an amorphous polymer, has low glass transition temperature and good rebound resilience, but has low mechanical strength, and can be used as a high-strength rubber material only by further crosslinking; the branched polyethylene with ultrahigh molecular weight has excellent wear resistance and mechanical property, but has overlarge Mooney viscosity and poor fluidity, and is not easy to process and mold; the branched polyethylene with proper molecular weight has good rebound resilience, lower Mooney viscosity, good fluidity and easy processing and forming; the linear polyethylene with ultrahigh molecular weight has super wear resistance and self-lubricating property, but is difficult to process. If, during the polymerization, a polyethylene having a low degree of branching and a high degree of branching can be produced simultaneously, it is possible to obtain a thermoplastic elastomer which does not require crosslinking and which can be reused; or in the polymerization process, highly branched polyethylene with medium-high molecular weight and ultrahigh molecular weight is generated simultaneously, so that the rubber material with good mechanical property, excellent wear resistance and easy molding processing can be obtained; or in the polymerization process, simultaneously generating the polyethylene with medium and low molecular weight and the highly branched polyethylene with ultrahigh molecular weight, and obtaining the thermoplastic elastomer which has good mechanical property and excellent wear resistance, is easy to form and process and does not need crosslinking; or in the polymerization process, the ultrahigh molecular weight and low branching degree polyethylene, the medium and high molecular weight highly branched polyethylene and the ultrahigh molecular weight highly branched polyethylene are simultaneously generated, so that the thermoplastic elastomer which has excellent mechanical properties and excellent wear resistance, is easy to mold and process and does not need crosslinking can be obtained. However, this goal is not achieved with only one (α -diimine) nickel olefin catalyst, which produces polyethylene with often relatively single properties.

Disclosure of Invention

The invention aims to overcome the defects of the prior art and provide an (alpha-diimine) nickel complex composition and application thereof. The composition is used for catalyzing ethylene polymerization, and can prepare a novel polyethylene material with excellent comprehensive performance.

In order to solve the technical problem, the solution of the invention is as follows:

providing an (alpha-diimine) nickel complex composition for catalyzing the polymerization of ethylene, the composition consisting of two or more of (alpha-diimine) nickel complexes A, B, C; wherein the content of the first and second substances,

the molecular structural formula of the (alpha-diimine) nickel complex A is shown as follows:

the molecular structural formula of the (alpha-diimine) nickel complex B is as follows:

the molecular structural formula of the (alpha-diimine) nickel complex C is as follows:

in the present invention, the (alpha-diimine) nickel complex A is used to catalyze ethylene to produce polyethylene having a branching degree of not less than 60 branches/1000 carbons and a weight average molecular weight of not more than 420 kg/mol; the (alpha-diimine) nickel complex B is used for catalyzing ethylene polymerization to generate polyethylene with the weight average molecular weight of 700-10000 kg/mol and the branching degree of 60-125 branched chains/1000 carbons; the (alpha-diimine) nickel complex C is used for catalyzing ethylene polymerization to generate polyethylene with the weight average molecular weight of 20-10000 kg/mol and the branching degree of 0-60 branched chains/1000 carbons.

In the present invention, the preparation process of the (α -diimine) nickel complex a is as follows:

the preparation method comprises the following specific steps:

(1) under the protection of nitrogen, carrying out dehydration condensation reaction of amino and carbonyl on 2 equivalents of aniline and 1 equivalent of methylglyoxal, monitoring the reaction end point by using thin-layer chromatography, stopping stirring after the reaction is completed, and vacuumizing to remove the solvent; separating and purifying by column chromatography to obtain alpha-diimine;

(2) under the anhydrous and oxygen-free conditions, complexing alpha-diimine with any one of ethylene glycol dimethyl ether nickel dibromide, ethylene glycol dimethyl ether nickel dichloride, nickel chloride tetrahydrate or nickel chloride hexahydrate to obtain the (alpha-diimine) nickel complex A.

In the present invention, the preparation process of the (α -diimine) nickel complex B is as follows:

the preparation method comprises the following specific steps:

(1) weighing ethylene substituted acenaphthenequinone 1,2, 6-di (diphenylmethyl) -4-methylaniline and ZnCl₂Putting into a flask, adding glacial acetic acid, fully stirring, heating to 120 ℃, and carrying out reflux reaction for 2 hours; after the reaction is finished, cooling the mixture to room temperature, filtering and separating to obtain a solid, and adding dichloromethane to completely dissolve the solid after washing; adding potassium oxalate solution and stirring vigorously for 30 minutes to generate zinc oxalate precipitate in a water phase; standing, collecting the upper organic layer, washing with deionized water, evaporating, and vacuum drying to obtain solidThe bulk powder is compound 2;

the molar ratio of the used amount of each raw material is as follows: ethylene substituted acenaphthenequinonediquinone 1: 2, 6-bis (diphenylmethyl) -4-methylaniline: ZnCl₂＝0.8∶1∶1；

(2) Taking compound 2 and ZnCl₂Putting into a flask, adding glacial acetic acid, fully stirring, and heating to 120 ℃; injecting 2, 6-diisopropylaniline, carrying out reflux reaction for 30 minutes, cooling to room temperature, filtering and separating to obtain a solid, washing, and adding dichloromethane to completely dissolve the solid; adding potassium oxalate solution and stirring vigorously for 30 minutes to generate zinc oxalate precipitate in a water phase; standing, collecting the upper organic layer, washing with deionized water, and adding anhydrous MgSO₄The powder was stirred overnight to remove residual moisture; filtering, evaporating the solvent to dryness, adding n-hexane for washing, and performing vacuum drying to obtain a solid powdery compound 3;

the molar ratio of the used amount of each raw material is as follows: compound 2: ZnCl₂2, 6-diisopropylaniline is 0.52: 0.7: 1;

(3) reacting (DME) NiBr₂Adding the compound 3 and dichloromethane into a sealed reaction bottle protected by nitrogen, and stirring and reacting for 24 hours at room temperature; pumping out dichloromethane, collecting the dichloromethane by using a cold trap, washing the dichloromethane by using ether, and pumping out the dichloromethane to obtain orange solid powder, namely the (alpha-diimine) nickel complex B;

the molar ratio of the used amount of each raw material is as follows: (DME) NiBr₂Compound 3 is 0.12: 0.125.

In the present invention, each of the (α -diimine) nickel complexes is used in combination of two or three in the following manner:

when the complex A and the complex B are combined, the molar ratio of the complex A to the complex B is 99: 1-50: 50;

when the complex A and the complex C are combined, the molar ratio of the complex A to the complex C is 99: 1-50: 50;

when the complex B and the complex C are combined, the molar ratio of the complex B to the complex C is 99: 1-1: 99;

when the three are used simultaneously, the molar ratio of the complex A to the complex B to the complex C is 100 (1-100) to 1-100.

The invention further provides an application method of the (alpha-diimine) nickel complex composition, which is to prepare a polyethylene material (NPE) by catalyzing ethylene polymerization by using the (alpha-diimine) nickel complex composition as a catalyst.

In the invention, in the process of catalyzing the ethylene polymerization, a cocatalyst is used, and the cocatalyst is a composition of alkyl metal and borate; wherein the content of the first and second substances,

the alkyl metal is one or more of trimethyl aluminum, triisobutyl aluminum, triethyl aluminum, diethyl aluminum chloride, ethyl aluminum dichloride, ethyl aluminum sesquichloride and diethyl zinc, and preferably diethyl aluminum chloride;

the borate is sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate, N-dimethylanilinium tetrakis (pentafluorophenyl) borate or triphenylmethyl tetrakis (pentafluorophenyl) borate, preferably sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate;

the molar ratio of the alkylaluminum borate to the diethyl zinc (α -diimine) nickel complex is 50 to 500:2 to 0.5:0 to 100: 1.

The invention also provides the use of the novel polyethylene material (NPE) prepared by the aforementioned process or of a composition comprising the novel polyethylene material (NPE) as, or in the manufacture of, any of the following: solar photovoltaic cell packaging adhesive films, conveyor belt cover stock, tire tread stock and films, at least one layer of a multilayer film, at least one layer of a laminate, a foamed article, a polypropylene impact modifier, a fiber, a nonwoven fabric, an injection molded article, a blow molded article, a rotational molded article, or an adhesive.

Description of the inventive principles:

the ortho positions of aniline substituent groups on the ligand of the complex A are two isopropyl groups with smaller volume ratio, the steric hindrance formed by the two isopropyl groups around the nickel metal at the active center is smaller, in the process of catalyzing ethylene polymerization, the polymer growing chain is easy to chain transfer to ethylene monomer, the molecular weight of the generated polyethylene is relatively lower, but the branching degree is higher, the fluidity of the polymer is good, the processing and forming performance is excellent, and the rebound resilience is good. The complex B is characterized in that on the basis of the complex A, a 2, 6-diisopropylaniline substituent on a ligand is changed into a 2, 6-diphenylmethyl-4-methylaniline substituent, and meanwhile, the skeleton of the ligand is changed into acenaphthylene. The asymmetric structure of the complex B enables steric hindrance around an active center of the complex B to be enlarged, molecular weight of polyethylene obtained by catalyzing ethylene polymerization is greatly improved, and meanwhile, higher branching degree is reserved. The polymerized product has excellent wear resistance and good rebound resilience, but has high Mooney viscosity and is not easy to process and mold. The ortho positions of the aniline substituent groups on the ligand of the complex C are two phenyl groups with larger volume ratio, so that the steric hindrance around the active center is large, the molecular weight of the polyethylene obtained by catalyzing ethylene polymerization is high, and the molecular weight of the polyethylene can be regulated and controlled in a wide range by regulating the polymerization temperature and pressure. However, the phenyl is a stronger power supply group, the electronegativity of the active center of the catalyst is obviously reduced, so that the chain walking capability of the catalyst is reduced, the branching degree of the polyethylene obtained by catalyzing ethylene polymerization is very low, and the polymerization product is easy to crystallize. Therefore, the complex A, B, C can be used in ethylene polymerization in combination of two or three, so as to generate polyethylene mixtures with different chain structures in situ, and different components exert respective characteristics, thereby endowing the polymerization product with excellent comprehensive performance.

Compared with the prior art, the invention has the beneficial effects that:

the (alpha-diimine) nickel complex composition is used for catalyzing ethylene polymerization, polyethylene mixtures with different chain structures can be generated in situ, and different components exert respective characteristics, so that excellent comprehensive performance is endowed to a polymerization product. This method of physical blending is not easy to achieve, especially the addition of refractory, poorly soluble ultra high molecular weight polyethylene to other polymers is more difficult to achieve by physical blending. Therefore, the (alpha-diimine) nickel complex composition is used for catalyzing ethylene polymerization, and the polyethylene with excellent comprehensive performance is prepared by an in-situ blending method, and has the advantages of simple production process, low production cost, high production efficiency and easiness in industrialization.

Drawings

FIG. 1 is a schematic diagram of the synthesis of (α -diimine) nickel complex A;

FIG. 2 is a single crystal structure of (α -diimine) nickel complex A with R being iPr;

FIG. 3 is a schematic diagram of the synthesis scheme of (α -diimine) nickel complex B;

FIG. 4 shows a single crystal structure of (. alpha. -diimine) nickel complex B.

Detailed Description

The invention provides an (alpha-diimine) nickel complex composition, which at least comprises more than two (alpha-diimine) nickel complexes, and is used for catalyzing ethylene polymerization, wherein the (alpha-diimine) nickel complex A catalyzes ethylene to generate polyethylene with the branching degree of not less than 60 branches/1000 carbons and the weight average molecular weight of not more than 420kg/mol, the (alpha-diimine) nickel complex B catalyzes ethylene to generate polyethylene with the weight average molecular weight of 700-10000 kg/mol and the branching degree of 60-125 branches/1000 carbons, and the (alpha-diimine) nickel complex C catalyzes ethylene to generate polyethylene with the weight average molecular weight of 20-10000 kg/mol and the branching degree of 0-60 branches/1000 carbons.

The (alpha-diimine) nickel complex composition, the molecular structural formula of the (alpha-diimine) nickel complex A, B and C is as follows:

in the synthesis process of the (alpha-diimine) nickel complex, the related ketoamine condensation reaction and coordination reaction are classical reactions in documents, and the reaction parameters such as the input amount of reactants and reaction conditions are common in the synthesis process, and are well known by researchers in the technical field. Synthetic references Organometallics of (α -diimine) nickel complex C, 2001,20 (11): 2321-2330.

The present invention will be further described with reference to the following specific examples, but the present invention is not limited to the following examples. The method is a conventional method unless otherwise specified. The starting materials are commercially available from the open literature unless otherwise specified.

Preparation of mono- (alpha-diimine) nickel complex A

Example 1

Under the protection of nitrogen, 2 equivalents of aniline and 1 equivalent of methylglyoxal are subjected to dehydration condensation reaction of amino and carbonyl, the end point of the reaction is monitored by thin-layer chromatography, after the reaction is completed, the stirring is stopped, and the solvent is removed by vacuumizing. Separating and purifying by column chromatography to obtain the alpha-diimine. Taking R as iPr (isopropyl), the characterization result of the alpha-diimine is as follows:¹³C NMR(100MHz,CDCl₃):167.87(C_Ph-N＝C),164.59(C_Ph-N＝C),148.14(C_Ph-N＝C),145.76(C_Ph-N＝C),136.84(C_Ph-CH),135.36(C_Ph-CH),124.87,124.40(C_Ph-H),123.22(C_Ph-H),28.53,28.30(CH(CH₃)₂),23.49,23.02(CH(CH₃)₂),15.94(N＝C－CH₃).

under the anhydrous and oxygen-free conditions, alpha-diimine is complexed with any one of ethylene glycol dimethyl ether nickel dibromide, ethylene glycol dimethyl ether nickel dichloride, nickel chloride tetrahydrate or nickel chloride hexahydrate to obtain the (alpha-diimine) nickel complex A. For example, the single crystal structure of complex a obtained by complexing α -diimine, in which R is iPr, with nickel ethylene glycol dimethyl ether dibromide is shown in fig. 2, and the single crystal data of (α -diimine) nickel complex a, in which R is iPr, is shown in table 1.

TABLE 1 Crystal Structure data of (alpha-diimine) Nickel Complex A with R being iPr

Preparation of di (alpha-diimine) nickel complexes B

Example 2

(1) 0.1665g (0.8mmol) ethylene substituted acenaphthenequinone 1, 0.4396g (1.0mmol)2, 6-bis (diphenylmethyl) -4-methylaniline, 0.1364g (1mmol) ZnCl were weighed out₂Put into a 100mL round-bottom flask, added with 25mL glacial acetic acid, stirred well, heated to 120 ℃, and reacted under reflux for 2 hours. After the reaction was complete, the mixture was cooled to room temperature to give a brick-red solid precipitate. The solid was isolated by filtration and washed with acetic acid (5 mL. times.3) and then ether (5 mL. times.3) to remove the remaining acetic acid. Will be provided withThe solid product was placed in a 100mL round bottom flask and 25mL of methylene chloride was added to dissolve completely, resulting in an orange-red solution. 0.2763g (1.5mmol) of potassium oxalate was weighed out and dissolved in 10mL of water, the potassium oxalate solution was poured into a round-bottomed flask and stirred vigorously for 30 minutes, and white zinc oxalate precipitated in the aqueous phase. Pouring the solution into a separating funnel, standing, after the solution is separated into upper and lower layers (the upper layer is an organic layer, and the lower layer is a water layer), taking the organic layer, washing the separated layer with deionized water (10mL multiplied by 3 times), evaporating the solvent by using a rotary evaporator, and putting the dried layer into a vacuum drying oven at 50 ℃ for drying to obtain brick red solid powder 2, weighing to obtain 0.3481g of product with mass and 79.1% of yield. The characterization results for compound 2 are as follows:¹H NMR(400MHz,CDCl₃,δ,ppm):8.07–6.40(m,26H,Ar-H),5.44(s,2H,CH(CH₃)₂),3.54–3.40(dd,4H,–CH₂–CH₂–),2.25(s,3H,CH₃)。ESI-MS:m/z 630.4([M+H]⁺)；652.4([M+Na]⁺)；668.4([M+K]⁺)。

(2) 0.3272g (0.52mmol) of Compound 2 and 0.0954g (0.7mmol) of ZnCl were weighed out₂Into a 100mL round-bottom flask, 25mL of glacial acetic acid was added, the mixture was stirred well, heated to 120 ℃ and 0.1173g (1.0mmol, about 0.19mL) of 2, 6-diisopropylaniline was added to the round-bottom flask by a one-shot syringe, and the mixture was refluxed for 30 minutes. After the reaction was complete, the mixture was cooled to room temperature to give an orange-red solid precipitate. The solid was isolated by filtration and washed with acetic acid (5 mL. times.3) and then ether (5 mL. times.3) to remove the remaining acetic acid. The solid product was charged into a 100mL round bottom flask, and 20mL of methylene chloride was added to dissolve completely, resulting in an orange-red solution. 0.1842g (1mmol) of potassium oxalate was weighed out and dissolved in 10mL of water, and the potassium oxalate solution was poured into a round-bottomed flask and stirred vigorously for 30 minutes, and white zinc oxalate precipitated in the aqueous phase. Pouring the solution into a separating funnel, standing, separating the solution from the upper layer and the lower layer (the upper layer is an organic layer and the lower layer is an aqueous layer), taking the organic layer, washing the organic layer with deionized water, separating the solution (10mL multiplied by 3 times), and adding 2 spoons of anhydrous MgSO (MgSO) into the solution₄The powder was stirred overnight to remove residual water. After filtration, the solvent was evaporated to dryness using a rotary evaporator, 15mL of n-hexane was added to the vessel, stirred for 15 minutes, filteredInsoluble solid was obtained by filtration, washed with n-hexane (5mL × 3 times), and dried in a vacuum oven at 50 ℃ to obtain Compound 3 as a orange-red solid powder, which was weighed to obtain 0.1032g in mass of product with a yield of 25.2%. The characterization of compound 3 is as follows:¹H NMR(500MHz,CDCl₃,δ,ppm):7.30–6.30(m,29H,Ar-H),5.68(s,2H,CH(CH₃)₂),3.42–3.31(dd,4H,–CH₂–CH₂–),3.21–3.11(sept,2H,CH(CH₃)₂),2.28(s,3H,CH₃),1.34–0.95(dd,12H,CH(CH₃)₂)。ESI-MS:m/z 789.4([M+H]⁺)；811.8([M+Na]⁺)。

(3) a50 mL Schlenk flask with a port and a 50mL reaction flask with a port were each charged with a vacuum oven bottle, evacuated three times with nitrogen, placed in a glove box, and 0.0372g (0.12mmol) of (DME) NiBr was weighed₂And 10mL of reflux purified methylene chloride was added to the Schlenk flask. 0.0985g (0.125mmol) of Compound 3 was added to a reaction flask under a nitrogen blanket, 10mL of dichloromethane (refluxing purification) was added to dissolve it, the solution was poured into a Schlenk flask with a disposable syringe, 5mL of dichloromethane (refluxing purification) was further added to the reaction flask to dissolve the remaining ligand, and the solution was also poured into a Schlenk flask. After the injection, the Schlenk flask was sealed with a sealing film and the reaction was stirred at room temperature for 24 hours. After the reaction started, the liquid in the Schlenk bottle was wine red with solid suspended matter. After 24 hours of reaction, stirring was stopped, and the dichloromethane in the Schlenk bottle was pumped dry and collected with a cold trap, washed with refluxing purified ether (10mL × 3 times), and then the ether was pumped dry for about 3 hours to give an orange solid powder, complex B. The single crystal structure of complex B is shown in fig. 4, and the single crystal data of (α -diimine) nickel complex B is shown in table 2.

TABLE 2 Crystal Structure data of (alpha-diimine) Nickel Complex B

Tri- (alpha-diimine) nickel complex compositions for catalyzing ethylene polymerization

Example 3

(alpha-diimine) nickel complex A catalyzed ethylene polymerization

The pressure polymerization of ethylene was carried out in a 300mL stainless steel autoclave manufactured by Buchi corporation. The reaction kettle is cleaned by n-heptane, the temperature in the kettle is raised to 90 ℃, then a vacuum pump is connected, and the reaction kettle is vacuumized for 2 hours at 90 ℃ to remove water and oxygen. Then the temperature is reduced to 40 ℃, the reaction kettle is vacuumized/charged with nitrogen and vacuumized/charged with ethylene respectively and pumped and discharged for three times, and finally the ethylene pressure in the kettle cavity is slightly more than 1 atm. 100mL of anhydrous and oxygen-free heptane solvent was injected into the kettle using a glass syringe, the electric stirrer was turned on to 300 rpm, and the cocatalyst of ethyl aluminum dichloride (Al: Ni: 200 (molar ratio)) was added. And finally, injecting 6mL of (alpha-diimine) nickel complex A solution (1mg/mL) dissolved in purified toluene in advance into the kettle cavity in a nitrogen environment by using a syringe which is pumped and discharged for six times, opening an ethylene gas flow valve, quickly adjusting a pressure reducing valve to the reaction pressure of 2.0MPa, and starting polymerization. And closing the flow valve after 30min to finish the polymerization reaction. The polymerization product is poured into acidified ethanol with 5% hydrochloric acid concentration to be stirred, and the polymer is settled until the liquid in the beaker is clear. The polymer precipitated was dried in a vacuum oven at 50 ℃ to constant weight, and the polymer product was collected. Polymerization Activity 1.68X 10⁷(PE)/mol (Ni). h, the weight-average molecular weight of the polyethylene obtained is 420kg/mol, the molecular weight distribution index is 2.8, the branching degree is 60 branches/1000 carbons, and the polyethylene obtained is numbered NPE-1. NPE-1 is dissolved in boiling tetrahydrofuran.

Example 4

(alpha-diimine) nickel complex A catalyzed ethylene polymerization

The polymerization temperature was raised to 60 ℃ and the amount of the cocatalyst ethyl aluminum dichloride was reduced (Al: Ni: 50 (molar ratio)), and N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate was added (B: Ni: 2 (molar ratio)) to reduce the polymerization pressure to 0.7MPa, as in example 3. Polymerization Activity 0.25X 10⁷g (PE)/mol (Ni). h, weight average molecular weight of the polyethylene obtained is 130kg/mol, molecular weight distribution index is 3.8, branching degree is 76 branches/1000 carbons, and numbering of the polyethylene obtainedDenoted as NPE-2. NPE-2 is dissolved in boiling tetrahydrofuran.

Example 5

(alpha-diimine) nickel complex A catalyzed ethylene polymerization

The cocatalyst was changed to diethylaluminum monochloride, (Al: Ni ═ 500 (molar ratio)) and triphenylmethyl tetrakis (pentafluorophenyl) borate (B: Ni ═ 1 (molar ratio)) was added, and the rest of the procedure was the same as in example 3. Polymerization Activity 0.18X 10⁷(PE)/mol (Ni). h, the weight-average molecular weight of the polyethylene obtained is 117kg/mol, the molecular weight distribution index is 3.0, the branching degree is 90 branches/1000 carbons, and the polyethylene obtained is numbered NPE-3. NPE-3 is dissolved in boiling tetrahydrofuran.

Example 6

(alpha-diimine) nickel complex B catalyzed ethylene polymerization

The catalyst was changed to (α -diimine) nickel complex B, and the rest was the same as in example 3. Polymerization Activity 4.36X 10⁷(PE)/mol (Ni). h, the weight average molecular weight of the polyethylene obtained is 10000kg/mol, the molecular weight distribution index is 2.0, the branching degree is 60 branches/1000 carbons, and the number of the polyethylene obtained is marked as NPE-4. NPE-3 is insoluble in boiling tetrahydrofuran.

Example 7

(alpha-diimine) nickel complex B catalyzed ethylene polymerization

The polymerization temperature was increased to 100 ℃ and the polymerization pressure was reduced to 0.7MPa, as in example 6. Polymerization Activity 1.01X 10⁷(PE)/mol (Ni). h, the weight-average molecular weight of the polyethylene obtained is 700kg/mol, the molecular weight distribution index is 2.4, the branching degree is 125 branches/1000 carbons, and the polyethylene obtained is numbered NPE-5. NPE-5 is dissolved in boiling tetrahydrofuran.

Example 8

(alpha-diimine) nickel complex B catalyzed ethylene polymerization

The polymerization temperature was lowered to 70 ℃ and the polymerization pressure was increased to 1.4MPa, as in example 6. Polymerization Activity 2.45X 10⁷(PE)/mol (Ni). h, the weight-average molecular weight of the polyethylene obtained is 2300kg/mol, the molecular weight distribution index is 2.2, the branching degree is 105 branches/1000 carbons, and the polyethylene obtained is numbered NPE-6. NPE-6 is soluble inBoiling tetrahydrofuran.

Example 9

(alpha-diimine) nickel complex C catalyzed ethylene polymerization

The catalyst was changed to (α -diimine) nickel complex C, as in example 3. Polymerization Activity 4.12X 10⁷(PE)/mol (Ni). h, the weight average molecular weight of the polyethylene obtained is 10000kg/mol, the molecular weight distribution index is 2.0, the branching degree is 0 branch/1000 carbons, and the number of the polyethylene obtained is marked as NPE-7. NPE-7 is insoluble in boiling tetrahydrofuran.

Example 10

(alpha-diimine) nickel complex C catalyzed ethylene polymerization

The polymerization temperature was increased to 100 ℃ and the polymerization pressure was reduced to 0.1MPa, as in example 9. Polymerization Activity 1.54X 10⁷(PE)/mol (Ni). h, the weight-average molecular weight of the polyethylene obtained is 20kg/mol, the molecular weight distribution index is 2.3, the branching degree is 60 branches/1000 carbons, and the polyethylene obtained is numbered NPE-8. NPE-8 is dissolved in boiling tetrahydrofuran.

Example 11

(alpha-diimine) nickel complex C catalyzed ethylene polymerization

The polymerization temperature was lowered to 70 ℃ and the polymerization pressure was increased to 1.4MPa, as in example 9. Polymerization Activity 2.89X 10⁷(PE)/mol (Ni). h, the weight average molecular weight of the polyethylene obtained is 3500kg/mol, the molecular weight distribution index is 2.1, the branching degree is 38 branches/1000 carbons, and the polyethylene obtained is numbered NPE-9. NPE-9 is insoluble in boiling tetrahydrofuran.

Example 12

(alpha-diimine) nickel complexes A and B compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex B is 99:1 (molar ratio), sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate is added (B: Ni molar ratio is controlled to 0.5), polymerization temperature is 60 ℃, ethylene pressure is 1.0MPa, and the rest is the same as in example 3. Polymerization Activity 0.43X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-10. NPE-10 is dissolved in boiling tetrahydrofuran. GPC results showed that NPE-10 has two GPC curvesOne peak corresponds to a weight average molecular weight of 210kg/mol, the molecular weight distribution index is 3.1, and the weight average molecular weight is the molecular weight and the distribution of the product of ethylene polymerization catalyzed by the (alpha-diimine) nickel complex A; the other peak had a weight average molecular weight of 1500kg/mol and a molecular weight distribution index of 2.1, which is the molecular weight and distribution of the product of the polymerization of ethylene catalyzed by the (alpha-diimine) nickel complex B. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 89% by mass and the latter being 11% by mass.

Example 13

(alpha-diimine) nickel complexes A and B compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a: (α -diimine) nickel complex B70: 30 (molar ratio), the remainder being as in example 4. Polymerization Activity 0.65X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-11. NPE-11 is dissolved in boiling tetrahydrofuran. GPC results showed that NPE-11 has two peaks in the GPC curve, one peak corresponding to a weight average molecular weight of 190kg/mol, a molecular weight distribution index of 2.8, the molecular weight and distribution of the product of the ethylene polymerization catalyzed by (alpha-diimine) nickel complex A; the other peak had a weight average molecular weight of 1550kg/mol and a molecular weight distribution index of 2.3, which is the molecular weight and distribution of the product of the ethylene polymerization catalyzed by the (alpha-diimine) nickel complex B. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 65% by mass and the latter being 35% by mass.

Example 14

(alpha-diimine) nickel complexes A and B compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a: (α -diimine) nickel complex B ═ 50:50 (molar ratio), the rest being as in example 5. Polymerization Activity 1.37X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-12. NPE-12 is dissolved in boiling tetrahydrofuran. GPC results showed that NPE-12 has two peaks in GPC curve, one peak corresponding to a weight average molecular weight of 220kg/mol, a molecular weight distribution index of 2.9, a molecular weight and distribution of the product of the ethylene polymerization catalyzed by (alpha-diimine) nickel complex A; in additionOne peak had a weight average molecular weight of 1510kg/mol and a molecular weight distribution index of 2.2, which is the molecular weight and distribution of the product of the (alpha-diimine) nickel complex B catalyzed ethylene polymerization. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 43% by mass and the latter 57% by mass.

Example 15

(alpha-diimine) nickel complexes A and C compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex C is 50:50 (molar ratio), sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate (B: Ni is controlled to 1 (molar ratio)) is added, the polymerization temperature is 70 ℃, the ethylene pressure is 1.0MPa, and the rest is as in example 3. Polymerization Activity 2.78X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-13. The NPE-13 can be separated into a tetrahydrofuran soluble component and a tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 41 percent, and the mass percent of the latter is 59 percent. The weight average molecular weight of the former is 170kg/mol, the molecular weight distribution index is 2.8, and the branching degree is 75 branches/1000 carbons; the latter had a weight average molecular weight of 2500kg/mol, a molecular weight distribution index of 2.4 and a degree of branching of 45 branches/1000 carbons.

Example 16

(alpha-diimine) nickel complexes A and C compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex C70: 30 (molar ratio), diethyl zinc (Zn: Ni 20 (molar ratio)) was added, and the remainder was the same as in example 15. Polymerization Activity 3.02X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-14. The NPE-14 can be separated into two parts of tetrahydrofuran soluble component and tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 59%, and the mass percent of the latter is 41%. The weight average molecular weight of the former is 150kg/mol, the molecular weight distribution index is 2.5, and the branching degree is 72 branches/1000 carbons; the latter had a weight average molecular weight of 2100kg/mol, a molecular weight distribution index of 2.2 and a degree of branching of 41 branches/1000 carbons.

Example 17

(alpha-diimine) nickel complexes A and C compositions catalyzed ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex C99: 1 (molar ratio), diethyl zinc (Zn: Ni is controlled to 100 (molar ratio)), and the remainder of example 15. Polymerization Activity 2.53X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-15. The NPE-15 can be separated into 75 percent by mass of tetrahydrofuran soluble component and 25 percent by mass of tetrahydrofuran insoluble component after being extracted for 12 hours by boiling tetrahydrofuran. The weight average molecular weight of the former is 130kg/mol, the molecular weight distribution index is 2.4, and the branching degree is 71 branches/1000 carbons; the latter had a weight average molecular weight of 1800kg/mol, a molecular weight distribution index of 2.3 and a degree of branching of 36 branches/1000 carbons.

Example 18

(alpha-diimine) nickel complexes B and C compositions catalyze ethylene polymerization

(α -diimine) nickel complex B (α -diimine) nickel complex C is 99:1 (molar ratio), polymerization temperature is 100 ℃, ethylene pressure is 1.0MPa, sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate (B: Ni is controlled to 1 (molar ratio)) is added, diethyl zinc (Zn: Ni is controlled to 20 (molar ratio)) is added, and the rest is the same as in example 3. Polymerization Activity 1.38X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-16. The NPE-16 can be separated into a tetrahydrofuran soluble component and a tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 92 percent, and the mass percent of the latter is 8 percent. The weight average molecular weight of the former is 830kg/mol, the molecular weight distribution index is 2.3, and the branching degree is 118 branches/1000 carbons; the latter had a weight average molecular weight of 2100kg/mol, a molecular weight distribution index of 2.2 and a degree of branching of 41 branches/1000 carbons.

Example 19

(alpha-diimine) nickel complexes B and C compositions catalyze ethylene polymerization

(alpha-diimine) nickel complex B (alpha-diimine) nickel complex C50: 50 (molar ratio), polymerization temperature 70 ℃, and the rest of the processExample 18. Polymerization Activity 1.97X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-17. The NPE-17 can be separated into two parts of tetrahydrofuran soluble component and tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 48%, and the mass percent of the latter is 52%. The weight average molecular weight of the former is 1690kg/mol, the molecular weight distribution index is 2.2, and the branching degree is 110 branches/1000 carbons; the latter had a weight average molecular weight of 2800kg/mol, a molecular weight distribution index of 2.2 and a degree of branching of 35 branches/1000 carbons.

Example 20

(alpha-diimine) nickel complexes B and C compositions catalyze ethylene polymerization

(α -diimine) nickel complex B: (α -diimine) nickel complex C is 1:99 (molar ratio), the rest being as in example 19. Polymerization Activity 2.39X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-18. The NPE-18 can be separated into two parts of tetrahydrofuran soluble component and tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 0.9 percent, and the mass percent of the latter is 99.1 percent. The weight average molecular weight of the former is 1700kg/mol, the molecular weight distribution index is 2.1, and the branching degree is 110 branches/1000 carbons; the latter had a weight average molecular weight of 2780kg/mol, a molecular weight distribution index of 2.2 and a degree of branching of 35 branches/1000 carbons.

Example 21

(alpha-diimine) nickel complex A, B and composition C catalyze ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex B (α -diimine) nickel complex C is 100:1:1 (molar ratio), polymerization temperature is 70 ℃, ethylene pressure is 1.4MPa, sodium tetrakis (3, 5-bis (trifluoromethyl) phenyl) borate (B: Ni is 1 (molar ratio)) is added, diethyl zinc (Zn: Ni is 20 (molar ratio)) is added, and the rest is the same as in example 3. Polymerization Activity 0.42X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-19. Extracting with boiling tetrahydrofuran for 12 hr to separate NPE-19 into tetrahydrofuran soluble component and tetrahydrofuran insoluble component, wherein the mass percentage of the former is 95%, and the mass percentage of the latter isThe content was 5%. GPC results show that the former GPC curve has two peaks, one peak corresponds to a weight average molecular weight of 260kg/mol, a molecular weight distribution index of 3.2, and is the molecular weight and the distribution of the product of ethylene polymerization catalyzed by the (alpha-diimine) nickel complex A; the other peak had a weight average molecular weight of 2350kg/mol and a molecular weight distribution index of 2.2, which is the molecular weight and distribution of the product of the (alpha-diimine) nickel complex B catalyzed ethylene polymerization. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 90% by mass and the latter being 10% by mass. The weight average molecular weight of the tetrahydrofuran insoluble component was 3560kg/mol, the molecular weight distribution index was 2.2, and the degree of branching was 36 branches/1000 carbons.

Example 22

(alpha-diimine) nickel complex A, B and composition C catalyze ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex B (α -diimine) nickel complex C is 100:50:50 (molar ratio), the remainder being as in example 21. Polymerization Activity 1.56X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-20. The NPE-20 can be separated into a tetrahydrofuran soluble component and a tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 43 percent, and the mass percent of the latter is 57 percent. GPC results show that the former GPC curve has two peaks, one peak corresponds to a weight average molecular weight of 258kg/mol, a molecular weight distribution index of 2.9, and is the molecular weight and the distribution of the product of ethylene polymerization catalyzed by the (alpha-diimine) nickel complex A; the other peak had a weight average molecular weight of 2280kg/mol and a molecular weight distribution index of 2.1, which is the molecular weight and distribution of the product of the polymerization of ethylene catalyzed by the (alpha-diimine) nickel complex B. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 58% by mass and the latter being 42% by mass. The weight average molecular weight of the tetrahydrofuran insoluble component was 3490kg/mol, the molecular weight distribution index was 2.0, and the degree of branching was 35 branches/1000 carbons.

Example 23

(alpha-diimine) nickel complex A, B and composition C catalyze ethylene polymerization

(α -diimine) nickel complex a (α -diimine) nickel complex B (α -diimine) nickel complex C in a molar ratio of 100:100:100, the remainder of example 21. Polymerization Activity 2.18X 10⁷g (PE)/mol (Ni). h, the polyethylene obtained is numbered NPE-21. The NPE-21 can be separated into two parts of tetrahydrofuran soluble component and tetrahydrofuran insoluble component by extracting with boiling tetrahydrofuran for 12 hours, wherein the mass percent of the former is 62%, and the mass percent of the latter is 38%. GPC results showed that the former GPC curve had two peaks, one peak corresponding to a weight average molecular weight of 262kg/mol, a molecular weight distribution index of 2.8, and the molecular weight and distribution of the product of ethylene polymerization catalyzed by (α -diimine) nickel complex A; the other peak had a weight average molecular weight of 2320kg/mol and a molecular weight distribution index of 2.3, which is the molecular weight and distribution of the product of the polymerization of ethylene catalyzed by the (alpha-diimine) nickel complex B. The relative amounts of the two components can be estimated by comparing the integrated areas of the two peaks, the former being 48% by mass and the latter being 52% by mass. The weight average molecular weight of the tetrahydrofuran insoluble component was 3520kg/mol, the molecular weight distribution index was 2.2, and the degree of branching was 35 branches/1000 carbons.

Examples of the applications

The application of the novel polyethylene material (NPE) provided by the invention in the photovoltaic industry is described by an application example.

The performance test method comprises the following steps:

(1) degree of crosslinking, peel strength: the determination is carried out according to the GB/T29848-2013 standard;

(2) light transmittance: the samples were tested according to the spectrophotometer method of GB/T2410-. The wavelength range of the spectrophotometer is set to 290nm to 1100 nm. Respectively calculating the average value of the light transmittance in the wave band range of 290 nm-380 nm and 380 nm-1100 nm. At least three samples were tested per group and the test results averaged. The light transmittance in the embodiment of the invention is a test result aiming at the wave band range of 380 nm-1100 nm.

(3) Volume resistivity: firstly, placing a sample in a laboratory with 23 +/-2 ℃ and 50% +/-5% RH for at least 48 h; and then testing the volume resistivity of the samples under the conditions of 1000V +/-2V and 60min of electrochemical time according to the requirements specified in GB/T1410-2006, testing 3 samples, and averaging the results.

(4) Resistance to wet heat aging and yellowing index: firstly, putting all samples into a high-temperature high-humidity aging test box, and setting test conditions as follows: the temperature is 85 ℃ plus or minus 2 ℃, and the relative humidity is 85 percent plus or minus 5 percent; the test time is 1000h, the sample is taken out after the test is finished, and after the sample is recovered for 2-4 h in an open environment with the temperature of 23 +/-5 ℃ and the relative humidity of less than 75%, appearance inspection is carried out, and no appearance defect is required; and finally, respectively measuring the yellow indexes of the laminated part samples before and after the test according to ASTM E313, wherein the yellow index of each sample is measured at least at 3 points, the yellow index of each sample is the average value of the measured points, and the change difference of the yellow indexes before and after aging is recorded.

(5) And (3) PID resistance performance test: the test was carried out at 85 ℃ and 85 RH% with a voltage of-1000V applied.

The formulation components of examples 1-10 are shown in tables 3 and 4: (wherein the parts by weight of the components used per 100 parts by weight of the polyethylene material (NPE) prepared according to the invention are listed).

TABLE 3 packaging composition formula (unit: parts by weight)

TABLE 4 packaging composition formulation (unit: parts by weight)

The encapsulating compositions of examples 1 to 10 were kneaded in an internal mixer, and then rolled or extruded to form a film having a film thickness of 0.5mm,

plate glass and a TFT backplane were attached to both surfaces of the film, respectively. The resulting laminate was then laminated in a vacuum laminator.

The performance test data for each test specimen is shown in table 5:

table 5 encapsulation composition performance test data

The examples 1-10 show that the packaging adhesive film with the NPE as the polymer matrix prepared by the invention has excellent transparency, and can ensure that a solar cell using the packaging adhesive film has good power generation efficiency.

Secondly, the packaging adhesive film with the NPE prepared by the invention as the polymer matrix has good peel strength with glass, high peel strength retention rate with the glass after moisture-heat aging resistance and low yellowing index, so that the packaging adhesive film with the NPE prepared by the invention as the polymer matrix has excellent adhesive property and moisture-heat aging resistance, and can be well applied to outdoor environment. The novel packaging adhesive film provided by the invention adopts polyethylene with a saturated hydrocarbon structure in all molecular chains, so that the novel packaging adhesive film has very high volume resistivity, has obvious advantages in the aspect of electrical insulation compared with EVA packaging adhesive films, and completely meets the performance requirements of the energy industry standard polyolefin elastomer (POE) packaging insulating adhesive film for crystalline silicon solar cell modules (NB/T10200-.

Example 11

Single glass solar module:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 100 parts by weight of NPE-13 (MI under a load of 2.16kg at 190 ℃ C. of 6.2g/10min), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidinyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing NPE-13 and the liquid components, then blending and extruding with the rest components in an extruder, controlling the extrusion temperature at 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the processes of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared by a lamination method at 145 ℃, wherein the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the TPT back sheet and the solar cell. And (3) anti-PID test: after 192 hours of testing, the output power attenuation degree is 0.83 percent.

Example 12

Single glass solar module:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 90 parts by weight of NPE-14(190 ℃, MI under a load of 2.16kg of 10g/10min), 10 parts by weight of a maleic anhydride-modified ethylene-1-octene copolymer (graft content of MAH of 1 wt%, MI: 1.5g/10min), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexylcarbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythrityl tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing all polymers and the liquid components, then blending and extruding the mixture with the rest components in an extruder, controlling the extrusion temperature at 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the processes of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared by a lamination method at 145 ℃, wherein the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the TPT back sheet and the solar cell. And (3) anti-PID test: after 192 hours of testing, the output power attenuation degree is 0.88%.

Example 13

Single glass solar module:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 70 parts by weight of NPE-15 (MI 15g/10min under a load of 2.16kg at 190 ℃), 30 parts by weight of Dow POE8137, 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing all polymers and the liquid components, then blending and extruding the mixture with the rest components in an extruder, controlling the extrusion temperature at 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the processes of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared by a lamination method at 145 ℃, wherein the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the TPT back sheet and the solar cell. And (3) anti-PID test: after 192 hours of testing, the output power attenuation degree is 0.83 percent.

Example 14

Single glass solar module:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 100 parts by weight of NPE-15 (MI 15g/10min under a load of 2.16kg at 190 ℃), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. The processing method comprises the following steps: all polymers, all silane coupling agents and peroxide with the weight of 10% of the silane coupling agent are uniformly mixed and then added into a double-screw extruder for blending and extrusion. The temperature of the feed end portion of the twin-screw extruder was 50 ℃, the temperature of the reactor portion into which nitrogen was injected was 210 ℃, and the temperature of the outlet after the reaction was 140 ℃ to obtain a graft-modified polymer base material a; and uniformly mixing the grafted and modified polymer matrix material A and the rest components, and extruding the mixture into a film by matching a double-screw extruder with a T-shaped die. Nitrogen was injected into the extruder and the extrusion temperature was controlled at 110 ℃. The mixture stays in the extruder for 4min, and the extrudate is subjected to casting film forming, cooling, slitting and coiling to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared by a lamination method at 145 ℃, wherein the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the TPT back sheet and the solar cell. And (3) anti-PID test: after 192 hours of testing, the output power attenuation degree is 0.86%.

Example 15

Two glass solar module, wherein battery module's two-layer glued membrane is transparent glue film:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 100 parts by weight of NPE-15 (MI 15g/10min under a load of 2.16kg at 190 ℃), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing NPE-15 and the liquid components, then blending and extruding with the rest components in an extruder, controlling the extrusion temperature at 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the processes of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared at 145 ℃ by a laminating method, wherein the solar cell is an N-type cell slice, and the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the glass cover plate and the solar cell. And (3) anti-PID test: after 192 hours of testing, the degree of output power attenuation is 0.65%.

Example 16

Double-glass solar module, its upper strata is transparent glue film, and the lower floor is the white film:

an upper encapsulant film with a thickness of 0.5mm was prepared from an encapsulant composition comprising: 100 parts by weight of NPE-15 (MI 15g/10min under a load of 2.16kg at 190 ℃), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing NPE-15 and the liquid components, then blending and extruding the mixture with the rest components in an extruder, controlling the extrusion temperature to be 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the procedures of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the transparent packaging adhesive film with the thickness of 0.5 mm.

A lower encapsulant film having a thickness of 0.5mm was prepared from an encapsulant composition comprising: 100 parts by weight of NPE-15 (MI under a load of 2.16kg at 190 ℃ C. is 15g/10min), 10 parts by weight of titanium dioxide powder, 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidinyl) sebacate, and 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. And (3) soaking and mixing the polymer matrix and the liquid components, blending and extruding the mixture with the rest components in an extruder, controlling the extrusion temperature to be 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and performing the processes of tape casting film forming, cooling, slitting and coiling on the extrudate to obtain the transparent packaging adhesive film with the thickness of 0.5 mm.

The solar cell module is prepared at 145 ℃ by a laminating method, wherein the solar cell is an N-type cell piece, the transparent packaging adhesive film is positioned between the upper layer glass cover plate and the solar cell, and the white film is positioned between the lower layer glass cover plate and the solar cell. And (3) anti-PID test: after 192 hours of testing, the degree of output power attenuation was 0.61%.

Example 17

Double-sided battery pack of two glass solar energy N type, wherein the battery is the double-sided battery of N type, and the two-layer glued membrane of subassembly is transparent adhesive film:

an encapsulating adhesive film having a thickness of 0.5mm was prepared from an encapsulating composition comprising: 100 parts by weight of NPE-15 (MI 15g/10min under a load of 2.16kg at 190 ℃), 1 part by weight of vinyltrimethoxysilane, 1 part by weight of t-butylperoxy-2-ethylhexyl carbonate, 0.5 part by weight of triallylisocyanurate, 0.05 part by weight of 4-hydroxy-TEMPO, 0.25 part by weight of pentaerythritol tetrakis (3, 5-di-t-butyl-4-hydroxy) phenylpropionate, 0.15 part by weight of bis (2,2,6, 6-tetramethyl-4-piperidyl) sebacate, 0.15 part by weight of 2-hydroxy-4-n-octyloxybenzophenone. Soaking and mixing NPE-15 and the liquid components, then blending and extruding with the rest components in an extruder, controlling the extrusion temperature at 90 +/-1 ℃, keeping the mixture in the extruder for 4min, and carrying out the processes of film casting, film forming, cooling, slitting and coiling on the extrudate to obtain the packaging adhesive film with the thickness of 0.5 mm. The solar cell module is prepared at 145 ℃ by a laminating method, wherein the solar cell is an N-type double-sided cell piece, and the packaging adhesive film is positioned between the glass cover plate and the solar cell and also positioned between the glass cover plate and the solar cell. And (3) anti-PID test: after 192 hours of testing, the output power attenuation degree is 1.45%.

In general, the packaging adhesive film taking the NPE prepared by the invention as the polymer matrix has excellent weather resistance, aging resistance, yellowing resistance, electrical insulation, good optical performance and bonding performance, and completely meets the use requirements of the photovoltaic industry.

The application of the novel polyethylene material (NPE) provided by the invention in the conveyor belt industry is described by an application example.

The performance test method comprises the following steps:

(1) and (3) hardness testing: testing by using a hardness tester according to the national standard GB/T531.1-2008, wherein the testing temperature is room temperature;

(2) and (3) testing the tensile strength and the elongation at break: according to the national standard GB/T528-2009, an electronic tensile testing machine is used for testing, the tensile speed is 500mm/min, the testing temperature is 23 +/-2 ℃, and the test sample is a 2-type dumbbell-shaped test sample;

(3) hot air accelerated aging test: according to the national standard GB/T3512-2001, the method is carried out in a thermal aging test box, and the temperature and the time are set according to actual conditions.

(4) Determination of abrasion resistance: according to the national standard GB 9867-88, the test is carried out by a rotary roller type abrasion machine method.

The formulation components for examples 18-24 are shown in Table 6: (wherein the parts by weight of the components used per 100 parts by weight of the polyethylene material (NPE) prepared according to the invention are listed)

TABLE 6 conveyer belt cover rubber formula

Example 18

Because the molecular weight of NPE-6 is too high, it is difficult to mix with internal mixer, so NPE-6 is directly made into sample according to test standard, and no additive is added. The relative volume abrasion loss of the material is 6.9mm through testing³The average relative volume abrasion loss of the natural rubber under the same conditions is only 3.4 percent of the abrasion loss of the standard rubber³It can be seen that the polyethylene prepared by ethylene polymerization catalyzed by the (alpha-diimine) nickel complex B provided by the invention is also an elastomer with excellent wear resistance.

Because the polyethylene prepared by catalyzing ethylene polymerization by the (alpha-diimine) nickel complex A provided by the invention has moderate molecular weight, low Mooney viscosity and good fluidity, the polyethylene prepared by catalyzing ethylene by the (alpha-diimine) nickel complex A and B is subjected to in-situ blending, on one hand, the processing performance of the polyethylene prepared by catalyzing ethylene polymerization by the (alpha-diimine) nickel complex B can be improved, and on the other hand, an elastomer with excellent wear resistance can be obtained. In addition, the (alpha-diimine) nickel complex C provided by the invention catalyzes ethylene polymerization at higher temperature and lower pressure to prepare polyethylene with lower molecular weight, lower branching degree, good fluidity and certain crystallinity. The composition of the (alpha-diimine) nickel complex A, B and C is used for ethylene polymerization, and the polyethylene prepared by catalyzing ethylene polymerization by the (alpha-diimine) nickel complex C can play a role of a plasticizer to improve the processability of a polymerization product, and can be easily crystallized at room temperature to improve the physical crosslinking point of the polymerization product, so that the thermoplastic elastomer with excellent wear resistance is provided.

Example 19 an elastomeric composition comprising NPE prepared according to the present invention was compounded as follows:

setting the temperature of an internal mixer at 70 ℃ and the rotating speed of 40 r/min, adding a polyethylene material (NPE) for prepressing and mixing for 30 seconds, then adding an oxide, a plasticizer, an antioxidant RD and polyethylene glycol, mixing for 2 minutes, then adding a reinforcing filler and paraffin oil, mixing for 2 minutes, finally raising the temperature in the internal mixer to 90 ℃, adding the other components, mixing for 2 minutes, discharging rubber, thinly passing on an open mill, then discharging sheets, and standing for 24 hours.

And (4) refining and discharging, preparing a tensile sample and a rotary roller abrasion sample according to a test standard, standing for 20 hours, and then carrying out performance test.

Example 20 an elastomeric composition comprising NPE prepared according to the present invention was compounded as follows:

setting the temperature of an internal mixer at 70 ℃ and the rotating speed of 40 r/min, adding a polyethylene material (NPE) for prepressing and mixing for 45 seconds, then adding an oxide, a plasticizer, an antioxidant RD and polyethylene glycol, mixing for 1 minute, then adding a reinforcing filler and paraffin oil, mixing for 1 minute, finally raising the temperature in the internal mixer to 95 ℃, adding the other components, mixing for 2 minutes, discharging rubber, thinly passing on an open mill, then discharging sheets, and standing for 24 hours.

And (4) refining and discharging, preparing a tensile sample and a rotary roller abrasion sample according to a test standard, standing for 20 hours, and then carrying out performance test.

Example 21 an elastomer composition comprising NPE prepared according to the present invention was compounded as follows:

setting the temperature of an internal mixer at 70 ℃ and the rotating speed of 40 r/min, adding a polyethylene material (NPE) for prepressing and mixing for 60 s, then adding an oxide, a plasticizer, an antioxidant RD and polyethylene glycol, mixing for 1 min, then adding a reinforcing filler and paraffin oil, mixing for 1 min, finally raising the temperature in the internal mixer to 105 ℃, adding the other components, mixing for 2 min, discharging rubber, thinly passing on an open mill, then discharging sheets, and standing for 24 h.

And (4) refining and discharging, preparing a tensile sample and a rotary roller abrasion sample according to a test standard, standing for 20 hours, and then carrying out performance test.

Examples 22-24 the elastomeric compositions containing NPE prepared according to the present invention were compounded as in example 19.

The results of the performance tests for examples 18-24 are shown in Table 7:

TABLE 7 conveyer belt cover rubber Performance test data

From the test results, the elastomer composition containing the NPE prepared by the invention not only has excellent wear resistance, but also is stable at a high temperature of 150 ℃, and completely meets the use requirements of the super-wear-resistant and high-temperature-resistant conveyor belt covering rubber.

The application of the novel polyethylene material (NPE) provided by the present invention in the tire industry will be described by way of an application example.

The formulation components for examples 25-30 are shown in Table 8: (wherein the parts by weight of the components used per 100 parts by weight of the polyethylene material (NPE) prepared according to the invention are listed)

TABLE 8 tire tread rubber formulation

Example 25 an elastomer composition comprising NPE prepared according to the present invention was compounded as follows:

step (1): first-stage mixing:

the first-stage mixing is carried out on an internal mixer or an open mill, and the first-stage mixing process comprises the following steps: firstly, NPE is put into an internal mixer or an open mill for mixing for 2 minutes, then silane coupling agent, plasticizer and white carbon black are added into a rubber mixing mill for mixing at 90 ℃, and then carbon black, anti-aging agent and paraffin are put into the rubber mixing mill for mixing at 100 ℃ for 2 minutes; primary rubber refining is obtained after primary refining;

step (2): and (3) second-stage mixing:

putting the primary rubber prepared in the step (1) on an open mill, after rubber materials wrap a roll, putting a cross-linking agent and a vulcanization accelerator into a rubber mixing machine, and mixing for 1.5 minutes at 50 ℃ to complete rubber mixing to obtain rubber mixing;

and (3): and (3) vulcanizing the rubber compound obtained in the step (2) on a flat vulcanizing machine, wherein the vulcanization temperature is 140 ℃, and the vulcanization time is 10 minutes.

Example 26 an elastomer composition comprising NPE prepared according to the present invention was compounded as follows:

step (1): first-stage mixing:

the first-stage mixing is carried out on an internal mixer or an open mill, and the first-stage mixing process comprises the following steps: firstly, NPE is put into an internal mixer or an open mill for mixing for 3 minutes, then silane coupling agent, plasticizer and white carbon black are added into a rubber mixing mill for mixing at 100 ℃, and then carbon black, anti-aging agent and paraffin are put into the rubber mixing mill for mixing at 110 ℃ for 2.5 minutes; primary rubber refining is obtained after primary refining;

step (2): and (3) second-stage mixing:

putting the primary rubber prepared in the step (1) on an open mill, after rubber materials wrap a roll, putting a cross-linking agent and a vulcanization accelerator into a rubber mixing machine, and mixing for 2 minutes at 55 ℃ to complete rubber mixing to obtain rubber compound;

and (3): and (3) vulcanizing the rubber compound obtained in the step (2) on a flat vulcanizing machine, wherein the vulcanization temperature is 160 ℃, and the vulcanization time is 15 minutes.

Example 27 an elastomeric composition comprising NPE prepared according to the present invention was compounded as follows:

step (1): first-stage mixing:

the first-stage mixing is carried out on an internal mixer or an open mill, and the first-stage mixing process comprises the following steps: firstly, NPE is put into an internal mixer or an open mill for mixing for 4 minutes, then silane coupling agent, plasticizer and white carbon black are added into a rubber mixing mill for mixing at 140 ℃, and then carbon black, anti-aging agent and paraffin are put into the rubber mixing mill for mixing at 120 ℃ for 3 minutes; primary rubber refining is obtained after primary refining;

step (2): and (3) second-stage mixing:

putting the primary rubber prepared in the step (1) on an open mill, after rubber materials are coated on a roller, putting a cross-linking agent and a vulcanization accelerator into a rubber mixing machine, and mixing for 3.5 minutes at 60 ℃ to complete rubber mixing to obtain rubber mixing;

and (3): and (3) vulcanizing the mixed rubber obtained in the step (2) on a flat vulcanizing machine, wherein the vulcanization temperature is 175 ℃, and the vulcanization time is 20 minutes.

Examples 28 to 30 the mixing method of the elastomer composition comprising NPE prepared by the present invention was the same as example 25.

The results of the performance tests for examples 25-30 are shown in Table 9:

TABLE 9 tire tread rubber Performance test data

From the test results, the elastomer composition containing the NPE prepared by the invention has excellent wear resistance and tensile property, and completely meets the use requirements of tire tread rubber.

Example 31

The novel polyethylene material obtained in inventive example 15 (NPE-13) was melted in an extruder, passed through an annular die, expanded with air, cooled, and cut into a biaxially oriented film having a thickness of 50 μm. The single-layer film prepared from the novel polyethylene material has high tear resistance and adhesion resistance, meets the requirements of GB/T4456-.

Example 32

A production line of three extruders (two extruders with a screw diameter of 33 mm and one extruder with a screw diameter of 25 mm) was used to prepare 3-layer cast films with a total thickness of 30 μm using a melt temperature of 205 c, a die width of 30 cm, a die gap of 0.8mm, a line speed of 18 m/min and a throughput of 6 kg/h. The three-layer film structure was an adhesive layer/core layer/barrier layer, wherein the adhesive layer (thickness 4.5 microns) was the novel polyethylene material (NPE-13) prepared in example 15 of the present invention, the core layer (thickness 21 microns) was linear low density polyethylene having a density of 0.918 g/cc and a melt index of 0.85 g/10min (190 ℃/2.16 kg), and the barrier layer (thickness 4.5 microns) was low density polyethylene having a density of 0.923 g/cc and a melt index of 0.75 g/10min (190 ℃/2.16 kg). The three-layer film has an adhesion of 85 grams, an elongation at break of 480%, and a puncture resistance at a deformation of 250% of 0.5 kg, and is useful for packaging of food products such as poultry, vegetables, fresh red meat, cheese, and non-food industrial and retail goods.

Example 33

100 parts of the novel polyethylene material prepared according to the invention as described in example 15 (NPE-13) are hot-melt mixed with 1.3 parts of azide blowing agent (AZ130, azodicarbonamide blowing agent), 2 parts of zinc oxide, 0.2 parts of stearic acid and 2 parts of peroxide crosslinking agent (di-tert-butylperoxyisopropylbenzene peroxide, 40% active on silica support, Perkadox (TM) 1440 peroxide), compression moulded into sheets and allowed to expand. Mixing conditions are as follows: rolling mill @130 ℃ for 10 minutes. The sheet from the roll mill was preheated in an oven to 90 ℃ for 15 minutes, then added to a mould preheated to 180 ℃, pressed and cured at this temperature for 10 minutes. When the sample is taken out, the sample is expanded to prepare a foaming product, the foaming product has lower shrinkage, lower compression set and higher split layer tearing and elongation, the performance of the foaming product meets the requirements of HG/T3082-2010 rubber soles, and the foaming product can be used in the fields of soles, floors, building materials and the like.

Example 34

The novel polyethylene material (NPE-13) prepared in example 15 of the present invention was spun in a fiber spinning line equipped with 24 25X 1mm spinnerets at a spinneret temperature of 260 deg.C, a melt temperature of 302 deg.C and a winding speed of 70 m/min into a multifilament bundle of 24 fibers having a circular cross-section, the tensile strength of the bundle being 8g/d, the modulus being 280g/d and the elongation at break being 850%, and the fiber material made of NPE was used in the fields of textile industry (including nonwoven fabrics), environmental protection, medicine and construction.

Example 35

The novel polyethylene material (NPE-14) prepared in the embodiment 16 of the invention is subjected to injection molding at a melting temperature of 200 ℃ to prepare a 60X 1 cubic centimeter plate, the tensile strength of the product is 34.5MPa, the elongation at break of the product is 1120%, and the product can be used for automobile interior parts such as automobile pillars of automobiles, household electrical appliances such as cover plates of washing machines, household equipment products such as toilet covers, injectors, bottles for containing powder and tablets.

Example 36

The novel polyethylene material (NPE-18) prepared according to the invention from example 20 was ground to a particle size of 150 to 500. mu.m, the rotomoulding was carried out in a test apparatus FSP M20 "Clamshell", the ground NPE-18 was placed in a cast aluminium mould, and the mould was rotated biaxially in a gas combustion oven. Hot air was circulated through the chamber by a blower while the temperature was increased to 288 ℃ in 4 minutes. The temperature was maintained for 15 minutes, the oven was then opened while still rotating and the mold was cooled with forced air circulation for 7 minutes, followed by water spray for 7 minutes and air cooling for an additional 2 minutes. The spindle speed was maintained at 6 rpm throughout the heating and cooling process, with a 4.5:1 spin ratio. After cooling, the mold is opened to take out the hollow object. The shrinkage rate of the rotational molding product is 2.25%, the maximum warpage is 1.42 mm, the impact strength at-40 ℃ is 10.5J/mm, and the rotational molding product can be used in the fields of tanks, containers, toys, boats, furniture, medical equipment, underground storage tanks, fuel tanks, mobile toilets, combination bathrooms, telephone kiosks, ship hulls, garbage cans, lamp covers, ice cans, device shells and the like.

Example 37

39 g of the novel polyethylene material prepared according to example 20 of the invention (NPE-18) were melted at 190 ℃ in a Haake Rheomix TM600 mixer, after which 17 g of paraffin oil were added, mixing was continued for 15 minutes, then the rotor was stopped, the drum was opened and the resulting blend was removed, flattened in a press and cooled. The resulting blend exhibits good oil eating properties, a Shore A hardness of 54, and a transition temperature of 86 ℃ as measured by thermomechanical analysis, and is useful in many soft elastomer applications, such as soft touch molding and pressure sensitive adhesives.

Example 38

6g of the novel polyethylene material prepared according to example 20 of the invention (NPE-18) and 49 g of isotactic polypropylene were melted in a Haake Rheomix TM600 mixer at 190 ℃ for 15 minutes, after which the rotor was stopped, the drum was opened and the resulting blend was removed. The normal temperature notch impact strength of the admixture reaches 53.81kJ/m²The flexural modulus is 620MPa, and the normal temperature notch impact strength of the corresponding isotactic polypropylene reaches 19.53kJ/m²The flexural modulus was 710MPa, indicating that NPE is an effective impact modifier for polypropylene.

Examples of applications or end uses

In view of the application of the novel polyethylene material (NPE) prepared by catalyzing ethylene polymerization with the (α -diimine) nickel complex composition or the composition comprising the novel polyethylene material (NPE) as the above-mentioned product or in the manufacture of the above-mentioned product, the present invention can be widely used in various fields of industry, military, medical hygiene, food, daily life, etc.

The polymers of the present invention are useful in a variety of conventional thermoplastic manufacturing processes to produce useful articles, including objects made by casting, calendering, blow molding or extrusion coating processes containing at least one film layer (e.g., at least one layer of a monolayer or multilayer film); an extrusion; molded articles, such as blow molded, injection molded, or rotational molded articles; fibers; and woven or non-woven fabrics. Thermoplastic compositions comprising the polymers of the present invention include blends with other natural or synthetic polymers, reinforcements, additives, flame retardant additives, stabilizers, antioxidants, colorants, crosslinkers, extenders, blowing agents, and plasticizers. Particularly useful are multicomponent fibers, such as core/sheath fibers, that contain an outer surface layer that at least partially comprises one or more polymers of the present invention.

Fibers that can be made from the polymers or blends of the present invention include staple fibers, multicomponent fibers, tows, sheath/core fibers, twisted fibers, and monofilaments. Suitable fiber forming methods include melt blow molding techniques, spin bonding, or spinning fibers from which woven or nonwoven fabrics can be obtained, or structures composed of such fibers, including blends with other fibers, such as nylon, polyester, or cotton, thermoformed articles, extruded profiles (including profile and co-extrusions), calendered articles, and drawn, twisted, or crimped yarns or fibers. The novel polymers described herein are also useful in wire and cable coating operations, as well as sheet extrusion, or rotational molding processes for vacuum forming operations. The composition comprising the NPE may also be formed into a finished article using conventional polyolefin processing techniques well known to those skilled in the art of polyolefin processing.

Dispersions (aqueous and non-aqueous) may also be formed using the NPE or formulations comprising the NPE of the invention. Foams comprising the NPE of the invention may also be formed. The NPE may also be crosslinked by any known means, for example using peroxides, silanes, electron beams, azides, or other crosslinking techniques. The NPE may also be chemically modified, for example by grafting (e.g., using maleic anhydride, silane, or other grafting agents), amination, halogenation, sulfonation, or other chemical modification.

Additives and adjuvants may be included in any formulation comprising the NPE of the invention. Suitable additives include fillers such as organic or inorganic particles (including clays, silica, talc, powdered metals), organic or inorganic fibers (including carbon fibers, steel wires or mesh, silicon nitride fibers, and nylon or polyester strands), nanoscale particles, clays, and the like; thickeners, extender oils, including paraffinic or naphthenic oils; and other natural and synthetic polymers, including other polymers of the present invention.

Suitable polymers for blending with the NPE of the invention include thermoplastic and non-thermoplastic polymers, including natural and synthetic polymers. Exemplary polymers for blending include polypropylene (impact modified polypropylene, isotactic polypropylene, atactic polypropylene, and atactic ethylene/propylene copolymers), various types of polyethylene, including low density polyethylene, high density polyethylene, linear low density polyethylene, metallocene polyethylene, including reactor type polyethylene (reactor type alloys of ziegler-natta polyethylene and metallocene polyethylene), ethylene-vinyl alcohol copolymer, ethylene-vinyl acetate copolymer, polystyrene, impact modified polystyrene, SBS, ABS, SEBS, and thermoplastic polyurethane. Homogeneous polymers such as olefin elastomers and elastomers, ethylene and propylene-based copolymers may also be used as components in blends comprising the NPE of the present invention.

Suitable end uses for the foregoing products include elastic films and fibers; adhesives (including hot melt adhesives and pressure sensitive adhesives); soft touch products such as toothbrush handles and implement handles; footwear (including soles and insoles); gaskets and profiles; automotive interior parts and profiles; foam products (open and closed cell); for impact modification of other thermoplastic polymers (e.g., high density polyethylene, isotactic polypropylene, or other olefin polymers); a bottle cap pad; coating the fabric; a hose; a weather strip; a pipe; a floor; and viscosity index improvers for lubricants, also known as pour point modifiers.

Thermoplastic compositions comprising a thermoplastic graft copolymer (especially isotactic polypropylene) and the NPE of the invention are particularly capable of forming core-shell type particles containing hard crystalline or semi-crystalline blocks, wherein the core is surrounded by soft or elastomeric blocks, thereby forming a "shell" around the enclosed regions of the hard polymer. These particles are formed and dispersed in the graft copolymer by the forces induced during the hot melt mixing or blending process. Upon curing, these regions become enclosed elastomeric particles encased in a polymer matrix.

Particularly preferred blends are thermoplastic elastomers (TPE), such as Thermoplastic Polyolefins (TPO), dynamically crosslinked thermoplastic elastomers (TPV) and styrene-based thermoplastic elastomers (SBS, SEBS). TPE and TPV blends can be prepared by combining the NPE of the invention (including functionalized or unsaturated derivatives thereof) with optional rubbers (including conventional block copolymers, especially SBS block copolymers) and optional crosslinking or vulcanizing agents. The above blends can be used in molded articles and optionally for crosslinking the resulting molded articles.

Suitable conventional block copolymers for this purpose have a Mooney viscosity (ML [email protected] ℃) of from 10 to 135, more preferably from 25 to 100, most preferably from 30 to 80. Suitable polyolefins include, inter alia, linear or low density polyethylene, polypropylene (including atactic, isotactic, syndiotactic and impact-modified forms thereof), and poly (4-methyl-1-pentene). Suitable styrene polymers include polystyrene, rubber-modified polystyrene, styrene/acrylonitrile copolymers (SAN), rubber-modified SAN, and styrene-maleic anhydride copolymers.

The blend may be prepared by mixing or kneading the individual components at about or above the melting point temperature of one or both of the components. For most NPEs, this temperature may be above 130 ℃, most typically above 145 ℃, and most preferably above 150 ℃. Typical polymer mixing or kneading equipment capable of achieving the desired temperature and melt plasticizing the mixture may be used. These include kneaders, mills, extruders (single screw and twin screw), banbury mixers, calenders, and the like. The order and method of mixing depends on the final composition. It is also possible to use a combination of a Banbury batch mixer and a continuous mixer, for example using a Banbury mixer, followed by a comminuting mixer, followed by an extruder. Typically, TPE or TPV compositions have a higher content of crosslinkable polymer (typically a conventional block copolymer containing unsaturated bonds) than TPO compositions. Generally, for TPE and TPV compositions, the weight ratio of NPE to block copolymer may be from 90:10 to 10:90, more preferably from 80:20 to 20:80, most preferably from 75:25 to 25: 75. For TPO compositions, the weight ratio of NPE to TPO may be from 49:51 to 5:95, more preferably from 35:65 to 10: 90. For the modified styrenic polymer, the weight ratio of NPE to polyolefin is 49:51 to 5:95, more preferably 35:65 to 10: 90.

The blend composition may comprise a processing oil, a plasticizer, and a processing aid. Rubber processing oils have a specific ASTM designation and paraffinic, naphthenic or aromatic processing oils are suitable. For every 100 parts total polymer, generally 0 to 150 parts, preferably 0 to 100 parts, most preferably 0 to 50 parts of oil are used. Higher amounts of oil may tend to improve the processability of the resulting product at the expense of some physical properties. Additional processing aids include conventional waxes, salts of fatty acids (e.g. calcium stearate or zinc stearate) (poly) alcohols (including ethylene glycol), (poly) alcohol ethers (including glycol ethers), (poly) esters (including (poly) propylene glycol) and their metal salts, especially group 1 or 2 metal salts or zinc salt derivatives.

Non-hydrogenated rubbers such as those comprising butadiene or isoprene in polymerized form, including block copolymers (hereinafter diene rubbers), have lower UV, ozone and oxidation resistance than predominantly or highly saturated rubbers. In applications such as tires made from compositions containing relatively high concentrations of diene rubber, it is known that the addition of carbon black together with an anti-ozone additive and an antioxidant can improve rubber stability. The fully saturated NPE of the present invention is particularly useful as a protective surface layer (coating, coextrusion or lamination) or weatherable film that adheres to articles made from conventional diene rubber modified polymer compositions.

For conventional thermoplastic elastomer applications, carbon black is an additive for UV absorption and stability properties. Representative examples of carbon blacks include ASTM N110, N121, N220, N231, N234, N242, N293, N299, S315, N326, N330, M332, N339, N343, N347, N351, N358, N375, N539, N550, N582, N630, N642, N650, N683, N754, N762, N765, N774, N787, N907, N908, N990 and N991. For many such uses, the NPEs of the invention and blends thereof require little or no carbon black, thereby creating considerable design freedom to include other alternative pigments or to use no pigment at all. Multi-tone tires matching vehicle colors are one possible use.

Compositions comprising the thermoplastic blends of the present invention may also contain antiozonants and antioxidants known to the ordinary rubber chemist. Antiozonants may be physical protectants, such as wax materials that coat the surface and protect the part from oxygen or ozone, or they may be chemical protectants that react with oxygen or ozone. Suitable chemoprotectants include styrenated phenols, butylated bis (dimethylbenzyl) phenol, butylated octylated phenols, p-phenylenediamine, p-cresol, and the butyl group of dicyclopentadieneA reaction product, a polyphenol antioxidant, a quinoline, a hydroquinone derivative, a diphenylene antioxidant, a thioester antioxidant, and blends thereof. Some typical tradenames for these products are Wingstay^TMS antioxidant, Polystay^TM100 antioxidant, Polystay^TM100AZ antioxidant, Polystay^TM200 antioxidant, Wingstay^TML antioxidant, Wingstay^TMLHLS antioxidant, Wingstay^TMK antioxidant, Wingstay^TM29 antioxidant, Wingstay^TMSN-1 antioxidant and Irganox^TMAn antioxidant. In some applications, the antioxidants and antiozonants used are preferably non-staining and non-migratory.

Hindered amine light stabilizers and UV absorbers may also be used in order to provide additional stability against UV radiation. Suitable examples include Tinuvin, available from Ciba Specialty Chemicals^TM 123、Tinuvin ^TM 144、Tinuvin ^TM 622、Tinuvin ^TM 765、Tinuvin ^TM 770、Tinuvin ^TM780 and Chemisorb available from Cytex Plastics, Houston TX, USA^TM T944。

For some compositions, additional mixing processes may be used to pre-disperse the antioxidants, antiozonants, carbon black, UV absorbers, and/or light stabilizers to form a masterbatch, and then form a polymer blend therefrom.

Suitable crosslinking agents (also referred to as vulcanizing agents) for use herein include sulfur-based, peroxide-based, or phenol-based compounds. When a sulfur-based vulcanizing agent is used, an accelerator and a vulcanization activator may also be used. Accelerators are used to control the time and/or temperature required for dynamic vulcanization and to improve the properties of the resulting crosslinked article. A single accelerator or a primary accelerator may be used. The total amount of primary accelerator may range from 0.5 to 4phr, preferably from 0.8 to 1.5, based on the total weight of the composition. It is also possible to use a primary accelerator in combination with a secondary accelerator, wherein the secondary accelerator is used in a minor amount, for example 0.05 to 3phr, in order to activate and improve the properties of the vulcanized article. The combined use of accelerators generally results in articles having somewhat better performance than articles made using the individual accelerators. In addition, delayed action accelerators may be used which are not affected by normal processing temperatures but produce satisfactory cures at ordinary curing temperatures. Vulcanization retarders may also be used. Suitable types of accelerators that can be used in the present invention are amines, guanidines, thioureas, thiazoles, thiurams, disulfides, sulfenamides, dithiocarbamates and xanthates. Preferably, the primary accelerator is a sulfenamide. If a second accelerator is used, the second accelerator is preferably a guanidine, dithiocarbamate or thiuram compound. Certain processing aids and curing activators may also be used. When a peroxide-based vulcanizing agent is used, a co-activator or co-agent, such as stearic acid and zinc oxide, may be used in combination therewith. Suitable coagents include trimethylolpropane triacrylate, trimethylolpropane trimethacrylate, triallylisocyanurate, triallylcyanurate. The use of peroxide crosslinkers and optional coagents for partial or complete dynamic vulcanization is well known in the art.

When a composition comprising NPE is at least partially crosslinked, the degree of crosslinking can be measured by dissolving the composition in a solvent for a specified duration and calculating the percentage of gel or non-extractable components. The percent gel generally increases with increasing degree of crosslinking. For the vulcanized article of the present invention, the gel content percentage is 5 to 100%.

The NPE of the invention and blends thereof have improved processability compared to prior art compositions because their unique branched chain structure reduces melt viscosity. Thus, the composition or blend exhibits improved surface appearance, particularly when formed into molded or extruded articles. At the same time, the present compositions and blends thereof uniquely have improved melt strength properties, thereby making the NPEs and blends thereof of the present invention, particularly TPO blends, useful in foam and thermoforming applications where melt strength is currently inadequate.

The thermoplastic composition of the invention may also contain organic or inorganic fillers or other additives such as starch, glass fibers, talc, calcium carbonate, aluminosilicates or aluminophosphates, nanoparticles (including nanotubes), wollastonite, graphite (including graphene), zeolites and ceramics such as silicon carbide, silicon nitride or titanium dioxide. Silane groups or other coupling agents may also be used for better filler adhesion.

The thermoplastic compositions of the present invention, including the aforementioned blends, can be processed by conventional molding techniques such as injection molding, thermoforming, extrusion, slush molding, insert molding, two-part overmolding, blow molding and others. Films, including multilayer films, can be made by casting or tentering processes, including blown film processes.

Test method

(1) High temperature GPC: a PL-220 type gel permeation chromatograph produced by British Polymer Laboratories is adopted, 10-15 mg of a sample is weighed and dissolved in 5ml of 1,2, 4-trichlorobenzene to prepare a solution with the concentration of 2-3 per mill. Heating at 160 deg.C for 3-4 hr to dissolve completely, filtering, and filtering with special filter gun to obtain 1 ml solution in special GPC test bottle. Three PLgel 1010 mu m MIXED-B type chromatographic columns are adopted in the test process, and the separation range of the chromatographic columns is 500-1 multiplied by 10⁷The method comprises the following steps of taking 1,2, 4-trichlorobenzene as a mobile phase, wherein the flow rate is 1.0 ml/min, the sample concentration is 2-3 mg/ml, and the test temperature is 150 ℃. Narrow-distribution polystyrene is used as a standard sample, a universal correction method is used for correcting data, and a polyethylene Mark-Houwink constant adopted in calculation is as follows: k is 1.56 × 10^-4，α＝0.76。

(2) Differential Scanning Calorimetry (DSC): a TA-Q200 differential scanning calorimeter from TA Instruments, USA, was used. Preparing a sample: weighing 3-5 mg of sample, placing the sample in a small crucible, compacting and placing the sample in a sample pool. And (3) testing: under the nitrogen protection atmosphere, the initial temperature is set to 40 ℃, the temperature is increased to 150 ℃ at the speed of 10 ℃/minute, the temperature is kept for 5 minutes to completely melt the sample, and the heat history is eliminated. Then the temperature is reduced to minus 80 ℃ at the speed of 20 ℃/minute, and the temperature is preserved for 5 minutes. Finally, the temperature is raised to 150 ℃ at the speed of 10 ℃/min, and a DSC curve is obtained. Data processing: crystallization temperature (T)_c) And enthalpy of crystallization (. DELTA.H)_crystal) Measured by a cooling curve, the glass transition temperature (T)_g) And enthalpy of fusion (. DELTA.H)_m) Can be measured from the second temperature rise curve, and the crystallinity x can be measured from Δ H_mDivided by the enthalpy of fusion of the perfectly crystalline polyethylene in the ideal state (292.6J/g).

(3) High temperature NMR: nuclear magnetic resonance Mercury Plus 300, manufactured by Varian corporation, USA, was used.

¹H-NMR:

Preparing a sample: about 15 mg of the sample was weighed out and then 0.5 ml of deuterated o-dichlorobenzene was added as a solvent. And (3) testing conditions are as follows: the temperature is 120 ℃, the sampling time is 1.998 seconds, the relaxation time is 1.0 second, the testing frequency is 300MHz, and 256 scans are carried out. The degree of branching of the polymer can be obtained by the following equation 1.1:

degree of branching 1000 × [2 (I)_CH3)/3(I_CH3+I_CH2+I_CH)](formula 1.1)

¹³C-NMR：

Preparing a sample: about 50 mg of sample is weighed and added into a nuclear magnetic tube, then a relaxation reagent accounting for 10% of the mass of the sample is added, and then 0.5 ml of deuterated o-dichlorobenzene is added as a solvent.

And (3) testing conditions are as follows: the temperature is 120 ℃, the sampling time is 0.8 second, the relaxation reagent is 3.0 seconds, the testing frequency is 300MHz, and the scanning times are 5000-10000. According to the polyethylene branch naming method proposed by Usami and Takiyama, the characteristic peaks in the carbon spectrum are assigned, and the degree of branching (in terms of the number of branches per 1000 carbons) and the proportion of branches are calculated according to the formulas 1.2 and 1.3:

N＝1000(I_Me/0.90+I_Et/0.84+I_Pr/0.83+I_Bu/0.90+I_Pe/0.90+I_Lg/0.80)/[I_main+5.5(I_Et/0.84)+I_Pr/0.83+8(I_Bu/0.90+I_Pe/0.90+I_Lg/0.80)](equation 1.2)

Methyl, ethyl, propyl, butyl, pentyl and C6 or more branched (I)_Me/0.90):(I_Et/0.84):(I_Pr/0.83):(I_Bu/0.90):(I_Pe/0.90):(I_Lg/0.80) (equation 1.3)

(4) Mixing and mechanical property testing of polymers

Mixing: an RM-200C Hapu torque rheometer was used. Weighing 40 g of sample, adding antioxidant with the mass of 3-5 per mill of the sample, and setting the mixing condition at 165 ℃, the rotation speed of 60 revolutions per minute and the mixing time of 6-8 minutes. After mixing, the sample is pressed into a film by a hot press at 165 ℃, and the film is cut by a cutter to prepare the dumbbell-shaped sample strip.

And (3) testing mechanical properties: the test is carried out by adopting an UTM-2103 type electronic tensile machine produced by Shenzhen New Sansi materials Limited. The tensile strength and the elongation at break were respectively measured by selecting the test method GB/T528 and the tensile rate 500 mm/min.