CN108003261B

CN108003261B - Method for polymerizing ethylene and polyethylene

Info

Publication number: CN108003261B
Application number: CN201610944742.9A
Authority: CN
Inventors: 亢宇; 张明森; 吕新平; 周俊领; 徐世媛; 张志会
Original assignee: Sinopec Beijing Research Institute of Chemical Industry; China Petroleum and Chemical Corp
Current assignee: Sinopec Beijing Research Institute of Chemical Industry; China Petroleum and Chemical Corp
Priority date: 2016-11-02
Filing date: 2016-11-02
Publication date: 2020-04-07
Anticipated expiration: 2036-11-02
Also published as: CN108003261A

Abstract

The invention relates to the field of polymerization reaction, and discloses an ethylene polymerization method and polyethylene obtained by the method, wherein the ethylene polymerization method comprises the following steps: the method comprises the following steps of carrying out polymerization reaction on ethylene in the presence of a catalyst under the condition of polymerization reaction, wherein the catalyst comprises a spherical porous mesoporous composite material and a magnesium salt and/or a titanium salt loaded on the spherical porous mesoporous composite material, and the spherical porous mesoporous composite material comprises a mesoporous molecular sieve material with a one-dimensional through pore channel structure and a mesoporous molecular sieve material with a hexagonal pore channel structure. The method uses a supported catalyst with stable mesoporous structure, and can obtain polyethylene products with lower bulk density and melt index and difficult breakage.

Description

Method for polymerizing ethylene and polyethylene

Technical Field

The invention relates to the field of polymerization reaction, in particular to a method for polymerizing ethylene and polyethylene prepared by the method.

Background

Since the synthesis of a regular mesoporous material with highly ordered pore channels by the company Mobile 1992, the mesoporous material has a high specific surface, a regular pore channel structure and a narrow pore size distributionThe application of the material in the fields of catalysis, separation, medicine and the like is greatly concerned. A novel mesoporous material SBA-15 is synthesized by Zhao Dongyuan et al in 1998, which has highly ordered pore diameter (6-30nm) and large pore volume (1.0 cm)³,/g), thicker pore walls (4-6nm), maintained high mechanical strength and good catalytic adsorption performance (see D.Y.ZHao, J.L.Feng, Q.S.Huo, et al Science 279(1998) 548-550). CN1341553A discloses a preparation method of a mesoporous molecular sieve carrier material, and the mesoporous material prepared by the method is used as a heterogeneous reaction catalyst carrier, so that the separation of a catalyst and a product is easy to realize.

However, the conventional ordered mesoporous material SBA-15 has a rod-like microscopic morphology, the flowability of the material is poor, and the high specific surface area and the high pore volume of the material cause the material to have strong water and moisture absorption capacity, so that the agglomeration of the ordered mesoporous material is further aggravated, and the storage, transportation, post-processing and application of the ordered mesoporous material are limited.

The development and application of polyethylene catalysts is a major breakthrough in the field of olefin polymerization catalysts after traditional Ziegler-Natta catalysts, which makes the research of polyethylene catalysts enter a rapidly developing stage. The homogeneous phase polyethylene catalyst has high activity, needs large catalyst consumption and high production cost, and the obtained polymer has no granular shape and cannot be used in a polymerization process of a slurry method or a gas phase method which is widely applied. An effective method for overcoming the above problems is to carry out a supporting treatment of the soluble polyethylene catalyst. At present, a great number of researches on the loading of polyethylene catalysts are reported. In order to develop new support/catalyst/cocatalyst systems in depth, it is necessary to develop different supports to drive the further development of the supported catalyst and polyolefin industries.

The mesoporous material of the supported polyethylene catalyst reported in the previous literature is MCM-41, and the catalytic activity of the MCM-41 which is treated by MAO and then supported by the polyethylene catalyst after ethylene polymerization is 10⁶gPE/(mol Zr h). The reason that the mesoporous material MCM-41 is loaded with the catalyst and then has lower ethylene polymerization activity is mainly that the thermal stability and the hydrothermal stability of the pore wall structure of the MCM-41 are poor, and the pore wall is partially arranged in the loading processThe molecular collapse affects the loading effect, so that the catalytic activity is affected.

Therefore, there is a need for a mesoporous material with a stable mesoporous structure, which can maintain an ordered mesoporous structure after loading an active component and has a supported catalyst with high catalytic activity, and which can improve the performance of polyethylene products.

Disclosure of Invention

The invention aims to overcome the defects of the prior art and provide an ethylene polymerization method and polyethylene, wherein a supported catalyst with stable mesoporous structure is used in the method, and a polyethylene product with low bulk density and melt index and difficult breakage can be obtained.

In order to achieve the above object, the present invention provides a method for polymerizing ethylene, comprising polymerizing ethylene in the presence of a catalyst under polymerization conditions, wherein the catalyst comprises a spherical porous mesoporous composite material and a magnesium salt and/or a titanium salt supported on the spherical porous mesoporous composite material, wherein the spherical porous mesoporous composite material comprises a mesoporous molecular sieve material having a one-dimensional through-channel structure and a mesoporous molecular sieve material having a hexagonal channel structure, the spherical porous mesoporous composite material has an average particle diameter of 21 to 29 μm, a specific surface area of 200 and 650 m/g, a pore volume of 0.5 to 1.8 ml/g, a trimodal pore size distribution, and the trimodal pore size corresponds to a first most probable pore size, a second most probable pore size, and a third most probable pore size, respectively, and the first most probable pore size is 1 to 10 nm, the second most probable pore size is 20-35 nm, and the third most probable pore size is 40-50 nm.

The invention also provides polyethylene prepared by the method.

The invention adopts the secondary ball milling technology and the cyclone separation technology in the spray drying technology, the secondary ball milling technology enables the obtained slurry to be more exquisite, the spherical particles obtained after spray drying have stable structure, can be repeatedly used as a catalyst carrier, have high strength and are not easy to break, and the preparation of the spherical porous mesoporous composite material does not need to use a binder, so that the structure of a sample can be prevented from being damaged in the process of removing the binder at high temperature. The obtained spherical porous mesoporous composite material has small particle size, uniform particle size distribution and narrow particle size distribution curve by adopting a cyclone separation technology, can avoid the agglomeration of the ordered mesoporous material in the use process, improves the fluidity of the ordered mesoporous material, and brings convenience to the storage, transportation, post-processing and application of the ordered mesoporous material.

In addition, the mesoporous structure of the spherical porous mesoporous composite material provided by the invention is stable, the ordered mesoporous structure can be still maintained after the active component is loaded, and the supported catalyst prepared by the mesoporous composite material has good fluidity. When the supported catalyst is used for ethylene polymerization reaction, a polyethylene product which has low bulk density and melt index and is not easy to break can be obtained, and specifically, the bulk density of the prepared polyethylene product is less than 0.5g/mL, the melt index is less than 0.5g/10min, and the breaking rate is less than 3 weight percent.

Additional features and advantages of the invention will be set forth in the detailed description which follows.

Drawings

The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention and not to limit the invention. In the drawings:

FIG. 1 is an X-ray diffraction pattern (XRD spectrum) of the spherical porous mesoporous composite material of example 1, with 2 θ on the abscissa and intensity on the ordinate;

FIG. 2 is a Scanning Electron Micrograph (SEM) of the spherical porous mesoporous composite material of example 1;

FIG. 3 is a particle size distribution curve of the spherical porous mesoporous composite material in example 1;

fig. 4 is a pore size distribution diagram of the spherical porous mesoporous composite material in example 1.

Detailed Description

The following describes in detail specific embodiments of the present invention. It should be understood that the detailed description and specific examples, while indicating the present invention, are given by way of illustration and explanation only, not limitation.

The endpoints of the ranges and any values disclosed herein are not limited to the precise range or value, and such ranges or values should be understood to encompass values close to those ranges or values. For ranges of values, between the endpoints of each of the ranges and the individual points, and between the individual points may be combined with each other to give one or more new ranges of values, and these ranges of values should be considered as specifically disclosed herein.

The present invention provides a process for the polymerization of ethylene, the process comprising: polymerizing ethylene in the presence of a catalyst under a polymerization condition, wherein the catalyst comprises a spherical porous mesoporous composite material and a magnesium salt and/or a titanium salt loaded on the spherical porous mesoporous composite material, the spherical porous mesoporous composite material comprises a mesoporous molecular sieve material with a one-dimensional through pore channel structure and a mesoporous molecular sieve material with a hexagonal pore channel structure, the average particle size of the spherical porous mesoporous composite material is 21-29 microns, the specific surface area is 200-650 square meters per gram, the pore volume is 0.5-1.8 milliliters per gram, the pore diameters are in a trimodal distribution, the trimodal corresponds to a first most probable pore diameter, a second most probable pore diameter and a third most probable pore diameter respectively, the first most probable pore diameter is 1-10 nanometers, and the second most probable pore diameter is 20-35 nanometers, the third mode pore size is 40-50 nm.

According to a preferred embodiment of the present invention, the average particle diameter of the spherical porous mesoporous composite material is 22-28 μm, the specific surface area is 220-300 square meters/g, the pore volume is 1.1-1.7 ml/g, the pore diameters are in a trimodal distribution, and the trimodal corresponds to the first most probable pore diameter of 6-9 nm, the second most probable pore diameter of 22-32 nm and the third most probable pore diameter of 42-50 nm, respectively;

according to a more preferred embodiment of the present invention, the spherical porous mesoporous composite has an average particle diameter of 23 to 27 μm, a specific surface area of 220-275 square meters per gram, a pore volume of 1.2 to 1.5 ml/gram, and a trimodal pore size distribution, wherein the trimodal pore size distribution corresponds to a first mode pore size of 7 to 8 nm, a second mode pore size of 24 to 31 nm, and a third mode pore size of 45 to 50 nm.

According to the present invention, in the catalyst, the contents of the spherical porous mesoporous composite and the magnesium salt and/or titanium salt supported on the spherical porous mesoporous composite are not particularly limited, and may be determined according to a supported catalyst that is conventional in the art. For example, the spherical porous mesoporous composite may be included in an amount of 90 to 99 wt%, and the sum of the contents of the magnesium salt and the titanium salt, in terms of magnesium element and titanium element, respectively, may be 1 to 10 wt%, based on the total weight of the catalyst. Preferably, the content of the spherical porous mesoporous composite material is 90.5-98.5 wt%, and the sum of the contents of the magnesium salt and the titanium salt calculated by the magnesium element and the titanium element respectively can be 1.5-9.5 wt%. More preferably, the content of the spherical porous mesoporous composite material is 91-96 wt%, and the sum of the contents of the magnesium salt and the titanium salt calculated by the magnesium element and the titanium element respectively is 4-9 wt%.

In the present invention, the kind of the magnesium salt and the titanium salt is not particularly limited, and may be conventionally selected in the art. For example, the magnesium salt may be one or more of magnesium chloride, magnesium sulfate, magnesium nitrate and magnesium bromide, preferably magnesium chloride; the titanium salt may be titanium tetrachloride and/or titanium trichloride.

In the invention, the content of each element in the catalyst component can be measured by adopting an X-ray fluorescence spectrum analysis method.

In the present invention, the catalyst may be prepared according to various methods conventionally used in the art, as long as a magnesium salt and/or a titanium salt is supported on the spherical porous mesoporous composite.

In a preferred case, the preparation method of the catalyst may include: in the presence of inert gas, the spherical porous mesoporous composite material is contacted with mother liquor containing magnesium salt and/or titanium salt.

Preferably, the conditions of the contacting include: the temperature is 25-100 ℃, preferably 40-60 ℃; the time is 0.1 to 5 hours, preferably 1 to 3 hours.

The mother liquor containing magnesium salt and/or titanium salt can be an organic solvent containing magnesium salt and/or titanium salt, the organic solvent can be isopropanol and tetrahydrofuran, and the volume ratio of tetrahydrofuran to isopropanol can be 1: 1-3, preferably 1: 1-1.5.

During the preparation of the catalyst, the magnesium salt and/or the titanium salt is preferably used in an excess amount with respect to the spherical porous mesoporous composite material. More preferably, the magnesium salt, the titanium salt and the spherical porous mesoporous composite material are used in such amounts that the sum of the contents of the magnesium salt and the titanium salt, respectively, in terms of magnesium element and titanium element, in the prepared supported catalyst, is 1-10 wt% and the content of the spherical porous mesoporous composite material is 90-99 wt%, based on the total weight of the catalyst. Preferably, the sum of the contents of the magnesium salt and the titanium salt calculated by magnesium element and titanium element respectively is 1.5-9.5 wt%, and the content of the spherical porous mesoporous composite material is 90.5-98.5 wt%. More preferably, the sum of the contents of the magnesium salt and the titanium salt calculated by magnesium element and titanium element respectively is 4-9 wt%, and the content of the spherical porous mesoporous composite material is 91-96 wt%.

In a preferred embodiment of the present invention, the magnesium salt and the titanium salt may be used in a weight ratio of 1:0.1 to 2, preferably 1: 0.5-2.

In the present invention, the preparation method of the catalyst further comprises: after the spherical porous mesoporous composite material is contacted with a mother solution containing magnesium salt and/or titanium salt, the composite material loaded with the magnesium salt and/or titanium salt is filtered and dried. The drying conditions are not particularly limited and may be drying means and conditions which are conventional in the art. Preferably, the preparation of the catalyst further comprises a washing process after filtration and before drying, and/or a milling process after drying. The washing and milling conditions can be selected by the person skilled in the art according to the practical circumstances and will not be described in detail here.

In the present invention, the inert gas is a gas which does not react with the raw materials and the product, and may be, for example, nitrogen gas or at least one of group zero element gases in the periodic table, preferably nitrogen gas, which is conventional in the art.

In the present invention, the spherical porous mesoporous composite does not contain a binder such as polyvinyl alcohol or polyethylene glycol.

In the present invention, the spherical porous mesoporous composite may further contain silica introduced through silica gel. The term "silica introduced through silica gel" refers to a silica component which is introduced into the finally prepared spherical porous mesoporous composite material from silica gel as a preparation raw material during the preparation of the spherical porous mesoporous composite material. In the spherical porous mesoporous composite material, the content of the silica introduced through the silica gel may be 1 to 200 parts by weight, preferably 20 to 180 parts by weight, and more preferably 50 to 150 parts by weight, with respect to 100 parts by weight of the total amount of the mesoporous molecular sieve material having the one-dimensional through-channel structure and the mesoporous molecular sieve material having the hexagonal channel structure.

According to the present invention, the spherical porous mesoporous composite material may be prepared by a method comprising the steps of:

(1) providing a mesoporous molecular sieve material with a one-dimensional through channel structure or preparing a filter cake of the mesoporous molecular sieve material with the one-dimensional through channel structure as a component a 1;

(2) providing a mesoporous molecular sieve material having a hexagonal pore structure or preparing a filter cake of a mesoporous molecular sieve material having a hexagonal pore structure as component a 2;

(3) providing silica gel or preparing a filter cake of silica gel as component b;

(4) mixing the component a1, the component a2 and the component b, performing first ball milling, mixing the obtained first ball milling slurry with water for pulping, performing second ball milling to obtain second ball milling slurry, performing spray drying on the second ball milling slurry, and screening by adopting a cyclone separation technology;

wherein, the average particle diameter of the spherical porous mesoporous composite material is 21-29 microns, the specific surface area is 200-650 square meters per gram, the pore volume is 0.5-1.8 ml/gram, the pore diameters are in trimodal distribution, the trimodal corresponds to a first most probable pore diameter, a second most probable pore diameter and a third most probable pore diameter respectively, the first most probable pore diameter is 1-10 nanometers, the second most probable pore diameter is 20-35 nanometers, and the third most probable pore diameter is 40-50 nanometers.

In the present invention, by controlling the particle size of the spherical porous mesoporous composite material within the above range, it can be ensured that the spherical porous mesoporous composite material is not easily agglomerated, and the conversion rate of reaction raw materials in the ethylene polymerization process can be improved by using the supported catalyst prepared by using the spherical porous mesoporous composite material as a carrier.

In the preparation process of the spherical porous mesoporous composite material, the pore size distribution of the spherical porous mesoporous composite material is controlled to be trimodal distribution mainly by controlling the composition of a mesoporous material filter cake (component a1 and component a2), and the microscopic morphology of the spherical porous mesoporous composite material is controlled to be spherical mainly by controlling a forming method (i.e. firstly, mixing the component a1, the component a2 and the component b, carrying out first ball milling, mixing the obtained first ball milling slurry with water for pulping, then carrying out second ball milling, obtaining second ball milling slurry, and carrying out spray drying on the second ball milling slurry).

According to the present invention, in the step (1), the process of preparing a filter cake of the mesoporous molecular sieve material having a one-dimensional through-channel structure may include: carrying out first mixing contact on a template agent, a silicon source, ethanol, trimethylpentane and an acid agent, and crystallizing and filtering a mixture obtained by the first mixing contact; the order of the first mixing and contacting is not particularly limited, and the template agent, the silicon source, the ethanol, the trimethylpentane and the acid agent may be mixed at the same time, or any two or three of them may be mixed, and then the other components may be added and mixed uniformly. According to a preferred embodiment of the present invention, the template agent, ethanol and acid agent are mixed uniformly, then trimethylpentane is added and mixed uniformly, and then a silicon source (for example, tetramethoxysilane) is added and mixed uniformly.

In the present invention, the amount of the template, ethanol, trimethylpentane and silicon source may vary within a wide range, for example, the molar ratio of the template, ethanol, trimethylpentane and silicon source may be 1: 100-500: 200-500: 50-200, more preferably 1: 180-400: 250-400: 70-150.

In the invention, the template can be various templates which are conventional in the field as long as the pore structure of the obtained spherical porous mesoporous composite material meets the requirement. For example, the templating agent may be a triblock copolymer polyoxyethylene-polyoxypropylene-polyoxyethylene. Wherein the templating agent is commercially available (e.g., from Aldrich under the trade name P123, formula EO)₂₀PO₇₀EO₂₀And Mn of 5800) or can be prepared by various conventional methods. When the template is polyoxyethylene-polyoxypropylene-polyoxyethylene, the number of moles of the template is calculated from the number average molecular weight of polyoxyethylene-polyoxypropylene-polyoxyethylene.

In the present invention, the silicon source may be various silicon sources conventionally used in the art. For example, the silicon source may be at least one of ethyl orthosilicate, methyl orthosilicate (also known as tetramethoxysilane), propyl orthosilicate, sodium orthosilicate, and silica sol, preferably tetramethoxysilane.

In the present invention, the acid agent may be various acidic aqueous solutions conventionally used in the art, and preferably, the acid agent is acetic acid and sodium acetate buffer solution having a pH of 1 to 6. The amount of the acid agent is not particularly limited, and may be varied within a wide range, and it is preferable that the pH value in the first mixing contact is 1 to 7.

In the present invention, the conditions of the first mixing contact are not particularly limited, and for example, the conditions of the first mixing contact generally include: the temperature can be 10-60 ℃, preferably 10-20 ℃; the time can be 10 to 72 hours, preferably 10 to 30 hours; the pH may be from 1 to 7, preferably from 3 to 6. In order to further facilitate uniform mixing between the substances, according to a preferred embodiment of the invention, the first mixing contact is carried out under stirring conditions.

In the present invention, the conditions for crystallization of the mixture obtained by the first mixing contact include: the temperature can be 30-150 ℃, preferably 40-80 ℃; the time may be 10 to 72 hours, preferably 20 to 30 hours. According to a preferred embodiment, the crystallization is carried out by hydrothermal crystallization.

In the step (1), in the above-described process of preparing a filter cake of a mesoporous molecular sieve material having a one-dimensional through-channel structure, the process of obtaining the filter cake by filtration may include: after filtration, repeated washing with deionized water (washing times may be 2 to 10) and suction filtration.

In the step (1), "providing the mesoporous molecular sieve material having a one-dimensional through channel structure" may be a product obtained by directly weighing or selecting the mesoporous molecular sieve material having a one-dimensional through channel structure, or may be a product obtained by preparing the mesoporous molecular sieve material having a one-dimensional through channel structure. The preparation method of the mesoporous molecular sieve material with the one-dimensional through channel structure can be implemented according to a conventional method, and for example, the preparation method can comprise the following steps: according to the method, the filter cake of the mesoporous molecular sieve material with the one-dimensional through channel structure is prepared, and then the obtained filter cake is dried.

According to the present invention, in the step (2), the process of preparing a filter cake of the mesoporous molecular sieve material having a hexagonal pore structure may include: and (3) carrying out second mixing contact on ethyl orthosilicate, hexadecyl trimethyl ammonium bromide and ammonia, and filtering a mixture obtained by the second mixing contact.

According to the present invention, in the process of preparing a filter cake of a mesoporous molecular sieve material having a hexagonal pore structure, the content of each substance can also be selected and adjusted within a wide range, for example, the molar ratio of the tetraethoxysilane, the hexadecyl trimethyl ammonium bromide and the ammonia can be 1: 0.1-1: 0.1 to 5, preferably 1: 0.2-0.5: 1.5-3.5.

In the present invention, the ammonia is preferably added in the form of aqueous ammonia. The aqueous ammonia of the present invention may be present in a concentration of 10 to 25% by weight.

In the present invention, the second mixed contacting process of tetraethyl orthosilicate, cetyltrimethylammonium bromide and ammonia is carried out in the presence of water. Preferably, part of the water is introduced in the form of aqueous ammonia and part of the water is added in the form of deionized water. In the second mixed contact system of tetraethoxysilane, hexadecyl trimethyl ammonium bromide and ammonia, the molar ratio of tetraethoxysilane to water can be 1:100-200, and is preferably 1: 120-180.

In the present invention, the conditions of the second mixing contact are not particularly limited, and may include, for example: the contact temperature is 25-100 ℃, preferably 50-90 ℃; the contact time is 2-8 hours, preferably 3-7 hours, and the pH may be 7.5-11, preferably 8-10. Preferably, the second mixing contact is carried out under agitation to facilitate uniform mixing between the substances.

In the above process of preparing a filter cake of the mesoporous molecular sieve material having a hexagonal pore structure, the process of obtaining the filter cake by filtration may include: after filtration, repeated washing with deionized water (washing times may be 2 to 10) and suction filtration.

According to the present invention, in the step (2), "providing the mesoporous molecular sieve material having a hexagonal pore structure" may be a product obtained by directly weighing or selecting the mesoporous molecular sieve material having a hexagonal pore structure, or may be a product obtained by preparing the mesoporous molecular sieve material having a hexagonal pore structure. The preparation method of the mesoporous molecular sieve material having a hexagonal pore structure may be performed according to a conventional method, and for example, the preparation method may include: a filter cake of a mesoporous molecular sieve material having a hexagonal pore structure is prepared according to the above method, and the resulting filter cake is then dried.

According to the present invention, in the step (3), the process of preparing the filter cake of silica gel may include: and carrying out third mixing contact on the water glass, the polyhydric alcohol and the inorganic acid, and filtering a mixture obtained by the third mixing contact.

In the present invention, the conditions of the third mixed contact are not particularly limited and may be appropriately determined according to a conventional process for preparing silica gel. For example, the conditions of the third mixing contact include: the temperature can be 10-60 ℃, preferably 20-40 ℃; the time may be 1 to 5 hours, preferably 1 to 3 hours; the pH value is 2-4. In order to facilitate uniform mixing of the materials, the third mixing contact process is preferably performed under stirring conditions.

In the present invention, the amounts of the water glass, the mineral acid and the polyol may vary within a wide range. For example, the weight ratio of water glass, mineral acid and polyol may be 1 to 8: 0.1-5: 1, preferably 3 to 6: 0.5-4: 1, more preferably 3 to 6: 1-3: 1.

in the present invention, the water glass is an aqueous solution of sodium silicate, and the concentration thereof may be 3 to 20% by weight, preferably 10 to 20% by weight. The inorganic acid may be various inorganic acids conventionally used in the art, and may be, for example, one or more of sulfuric acid, nitric acid, and hydrochloric acid. The inorganic acids can be used in pure form or in the form of their aqueous solutions, preferably in the form of 3 to 20% by weight aqueous solutions. The inorganic acid is preferably used in such an amount that the pH of the contact reaction system of the water glass and the inorganic acid is 2 to 4.

In the present invention, the kind of the polyol is not particularly limited, and for example, it may be glycerin and/or ethylene glycol, and glycerin is preferable.

According to the invention, in the step (3), "providing silica gel" may be directly weighing or selecting the silica gel product, or preparing silica gel. The method for preparing silica gel may be carried out according to conventional methods, and may include, for example: a filter cake of silica gel was prepared according to the above method and the resulting filter cake was then dried.

In the above process for preparing a filter cake of silica gel, the process for obtaining the filter cake by filtration may include: after filtration, washing is carried out until the content of sodium ions is 0.2 wt% or less, preferably 0.01 to 0.03 wt%, and then suction filtration is carried out. The washing method is a routine choice in the field, and can be water washing and/or alcohol washing, and the specific conditions are well known to those skilled in the art and are not described in detail herein.

According to the present invention, in step (4), the amount of the component a1, the component a2 and the component b may be varied within a wide range, for example, the amount of the component b may be 1 to 200 parts by weight, preferably 20 to 180 parts by weight, more preferably 50 to 150 parts by weight, relative to 100 parts by weight of the total amount of the component a1 and the component a 2; the component a1 and the component a2 may be used in a weight ratio of 1:0.1 to 10, preferably 1:0.5 to 2.

In order to improve the strength of the spherical porous mesoporous composite material and further improve the performance of the prepared polyethylene product, the invention is realized by a secondary ball milling method of slurry.

According to the present invention, in the step (4), the first ball milling and the second ball milling may be performed in a ball mill in which the inner wall of a ball milling jar is preferably an agate inner liner, and the diameter of the milling balls in the ball mill may be 2-3 mm; the number of the grinding balls can be reasonably selected according to the size of the ball milling tank, and for the ball milling tank with the size of 50-150mL, 1 grinding ball can be generally used; the material of the grinding ball can be agate, polytetrafluoroethylene and the like, and agate is preferred. The conditions of the first ball milling and the second ball milling can be the same or different, and the conditions of the first ball milling and the second ball milling respectively and independently comprise: the rotation speed of the grinding ball can be 200-; preferably, the rotation speed of the grinding balls is 300-.

According to the invention, in the step (4), the temperature for mixing the obtained first ball-milling slurry with water for pulping can be 25-60 ℃, and the weight ratio of the first ball-milling slurry to the water can be 1:0.1 to 5, preferably 1: 0.5-3.5.

According to the present invention, in the step (4), the spray drying may be performed according to a conventional manner, and may be selected from at least one of a pressure spray drying method, a centrifugal spray drying method, and a pneumatic spray drying method. According to a preferred embodiment of the present invention, the spray drying is a centrifugal spray drying method. The spray drying may be carried out in an atomizer. The conditions of the spray drying may include: the temperature is 150-; preferably, the spray drying conditions include: the temperature is 150-250 ℃, and the rotating speed is 11000-13000 r/min.

According to the invention, the step of screening the second ball-milling slurry by adopting a cyclone separation technology after spray drying comprises the following steps: and carrying out spray drying on the second ball-milling slurry, and carrying out cyclone separation on the discharged gas containing the powder particles so as to collect the powder particles. Specifically, the cyclone separation technology is adopted to separate the powder particles contained in the discharged gas, the recovered powder particles fall into the powder collecting cylinder, the waste gas is delivered to the centrifugal fan from the outlet of the separator, the butterfly valve is installed at the lower part of the cyclone separator, and when the cyclone separator works, the butterfly valve is opened, and the obtained sample has uniformly distributed particle sizes.

According to the present invention, in the step (4), when the component a1 is a filter cake of a mesoporous molecular sieve material having a one-dimensional through-channel structure, the component a2 is a filter cake of a mesoporous molecular sieve material having a hexagonal-channel structure, and the component b is a filter cake of silica gel, that is, when the step (1) is a process of preparing a filter cake of a mesoporous molecular sieve material having a one-dimensional through-channel structure, the step (2) is a process of preparing a filter cake of a mesoporous molecular sieve material having a hexagonal-channel structure, and the step (3) is a process of preparing a filter cake of silica gel, the preparation method of the spherical porous mesoporous composite material may further include: after the spray drying process of step (4), the templating agent is removed from the powder particles collected by cyclone separation. The conditions for removing the template agent comprise: the temperature can be 90-600 ℃, preferably 300-600 ℃; the time may be 10 to 80 hours, preferably 10 to 24 hours.

According to the present invention, the conditions of the polymerization reaction may be those conventional in the art. For example, the polymerization reaction is carried out in the presence of an inert gas under conditions comprising: the temperature can be 10-100 ℃, the time can be 0.5-5h, and the pressure can be 0.1-2 MPa; preferably, the temperature is 20-95 ℃, the time is 1-4h, and the pressure is 0.5-1.5 MPa; further preferably, the temperature is 70-85 ℃, the time is 1-2h, and the pressure is 1-1.5 MPa.

The pressure referred to herein is gauge pressure.

In the present invention, the polymerization reaction may be carried out in the presence of a solvent, and the solvent used in the polymerization reaction is not particularly limited, and may be, for example, hexane.

According to the present invention, in a preferred aspect, a process for the polymerization of ethylene comprises: under the condition of polymerization reaction, in the presence of catalyst and adjuvant making ethylene undergo the process of polymerization reaction; preferably, the adjuvant is an alkyl aluminium compound.

In the present invention, the alkyl aluminum compound has a structure represented by formula I:

AlR_nX⁵ _(3-n)formula I

In the formula I, R may be each C₁-C₅Alkyl groups of (a); x⁵May each be one of the halogen groups, preferably-Cl; n is 0, 1, 2 or 3.

Preferably, said C₁-C₅The alkyl group of (a) may be one or more of methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl, tert-pentyl and neopentyl.

In the present invention, specific examples of the alkyl aluminum compound include, but are not limited to: trimethylaluminum, dimethylaluminum chloride, triethylaluminum, diethylaluminum chloride, tri-n-propylaluminum, di-n-propylaluminum chloride, tri-n-butylaluminum, tri-sec-butylaluminum, tri-tert-butylaluminum, di-n-butylaluminum chloride and diisobutylaluminum chloride. Most preferably, the alkyl aluminium compound is triethyl aluminium.

In the present invention, the amount of the alkyl aluminum compound may also be selected conventionally in the art, and in general, the mass ratio of the alkyl aluminum compound to the amount of the catalyst may be 1:0.1 to 10; preferably, the mass ratio of the alkyl aluminum compound to the catalyst is 1: 0.2 to 8; more preferably 1: 0.4-4.

In the invention, the ethylene polymerization method can further comprise the step of performing suction filtration separation on the final reaction mixture after the polymerization reaction is finished, so as to obtain the polyethylene granular powder.

The invention also provides polyethylene prepared by the method.

The present invention will be described in detail below by way of examples.

In the following examples and comparative examples, polyoxyethylene-polyoxypropylene-polyoxyethylene was obtained from Fuka under the trade name Synperonic F108 and has the formula PEO₁₃₂-PPO₅₀-PEO₁₃₂Average molecular weight M_n＝14600。

In the following examples and comparative examples, X-ray diffraction analysis was carried out on an X-ray diffractometer, model D8Advance, available from Bruker AXS, Germany; scanning electron microscopy analysis was performed on a scanning electron microscope, model XL-30, available from FEI, USA; pore structure parameter analysis was performed on a nitrogen desorption apparatus model Autosorb-1 available from corna, usa, wherein the sample was degassed at 200 ℃ for 4 hours before testing; the X-ray fluorescence analysis is carried out on an X-ray fluorescence analyzer with the model of Axios-Advanced of the Netherlands company; the particle size distribution curve was measured by a malvern laser particle sizer.

The bulk density of the polyolefin powder was determined by the method specified in GB/T1636-2008.

Polymer melt index: measured according to ASTM D1238-99.

Crushing rate of polyethylene granular powder: and (3) screening and measuring by using a 800-mesh screen, specifically, passing the polyethylene granular powder through the 800-mesh screen, wherein the crushing rate is the percentage of the weight of the polyethylene granular powder which passes through the 800-mesh screen to the weight of the polyethylene granular powder to be tested.

Example 1

This example illustrates the ethylene polymerization process and the polyethylene obtained according to the invention

(1) Preparation of spherical porous mesoporous composite material

Adding 1g (0.00017mol) of template P123 and 1.69g (0.037mol) of ethanol into 28mL of acetic acid and sodium acetate buffer solution with the pH value of 4.4, stirring at 15 ℃ until the template is completely dissolved, adding 6g (0.05mol) of trimethylpentane into the solution, stirring at 15 ℃ for 8 hours, adding 2.13g (0.014mol) of tetramethoxysilane into the solution, stirring at 15 ℃ for 20 hours, transferring the solution into an agate-lined reaction kettle, oven-crystallizing at 60 ℃ for 24 hours, filtering, washing with deionized water for 4 times, and suction-filtering to obtain a filter cake A11 of the mesoporous molecular sieve material with a one-dimensional through pore structure.

Adding hexadecyl trimethyl ammonium bromide and ethyl orthosilicate into an ammonia water solution with the concentration of 25 weight percent at the temperature of 80 ℃, and then adding deionized water, wherein the adding amount of the ethyl orthosilicate is 1g, and the mol ratio of ammonia to water in the ethyl orthosilicate, the hexadecyl trimethyl ammonium bromide and the ammonia water is 1: 0.37: 2.8: 142 and stirred at a temperature of 80 ℃ for 4 hours, after which the solution is filtered with suction and washed four times with distilled water, giving a filter cake a12 of mesoporous molecular sieve material having a hexagonal pore structure.

Mixing 15 wt% of water glass, 12 wt% of sulfuric acid solution and glycerol in a weight ratio of 4: 1:1 at 40 ℃ for 1 hour, then adjusting the pH to 3 with 98% by weight sulfuric acid, then suction-filtering the resulting reaction mass, and washing with distilled water until the sodium ion content is 0.02% by weight, to give a silica gel cake B1.

And (3) putting 5g of the prepared filter cake A11, 5g of the prepared filter cake A12 and 10g of the prepared filter cake B1 into a 100mL ball milling tank together, wherein the ball milling tank is made of agate, the grinding balls are made of agate, the diameter of each grinding ball is 3mm, the number of the grinding balls is 1, and the rotating speed is 400 r/min. And sealing the ball milling tank, and carrying out first ball milling in the ball milling tank at the temperature of 25 ℃ for 5 hours. The obtained first ball-milled slurry was mixed with 40g of water at 25 ℃ for pulping, followed by second ball milling at 25 ℃ for 5 hours. And (3) spray-drying the obtained second ball-milling slurry at the temperature of 200 ℃ at the rotating speed of 12000r/min, then screening by adopting a cyclone separation technology, calcining the screened product in a muffle furnace at the temperature of 550 ℃ for 10h, and removing P123 (template) to obtain the spherical porous mesoporous composite material C1.

The spherical porous mesoporous composite material C1 is characterized by XRD, a scanning electron microscope and a nitrogen adsorption instrument.

Fig. 1 is an X-ray diffraction pattern, and it can be seen that the spherical porous mesoporous composite material C1 has a mesoporous structure specific to a mesoporous material.

FIG. 2 is a SEM image of the spherical porous mesoporous composite C1, and it can be seen that the spherical porous mesoporous composite C1 has a micro-morphology of microspheres with a particle size of 21-29 μm and has good dispersibility.

Fig. 3 is a particle size distribution curve of the spherical porous mesoporous composite C1, and it can be seen that the spherical porous mesoporous composite C1 has a uniform particle size distribution.

Fig. 4 is a pore size distribution diagram of the spherical porous mesoporous composite material C1, and it can be seen from the diagram that the spherical porous mesoporous composite material C1 has a porous structure distribution and uniform pore channels.

The pore structure parameters of the spherical porous mesoporous composite material C1 are shown in table 1 below.

TABLE 1

*: the first most probable aperture, the second most probable aperture, and the third most probable aperture are separated by commas: the first most probable aperture, the second most probable aperture and the third most probable aperture are arranged in the order from left to right.

(2) Preparation of the catalyst

0.1g of magnesium chloride and 0.1g of titanium tetrachloride were dissolved in 10mL of a composite solvent of tetrahydrofuran and isopropanol (the volume ratio of tetrahydrofuran to isopropanol was 1: 1.2) to form a catalyst mother liquor. 1g of spherical porous mesoporous composite material C1 was added to the mother liquor at 45 ℃ and immersed for 1h, then filtered, and washed with n-hexane for 4 times, dried at 75 ℃ and ground to obtain catalyst D1.

As a result of X-ray fluorescence analysis, the catalyst D1 obtained in this example had a magnesium element content of 7.0 wt% and a titanium element content of 1.6 wt%, calculated as elements.

(3) Ethylene polymerization

In a 2L stainless steel high pressure polymerization reactor, nitrogen and ethylene were each replaced three times, then 200mL of hexane was added, the reactor was warmed to 80 ℃ and 800mL of hexane was added, 2mL of a 1mol/L Triethylaluminum (TEA) solution in hexane was added with the addition of hexane, then 0.5g of catalyst component D1 was added, ethylene gas was introduced, the pressure was raised to 1.0MPa and maintained at 1.0MPa, and after 1 hour of reaction at 70 ℃, separation by suction filtration was carried out to obtain a polyethylene pellet powder. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

Example 2

(1) Preparation of spherical porous mesoporous composite material

Adding 1g (0.00017mol) of template P123 and 1.4g (0.03mol) of ethanol into 28mL of acetic acid and sodium acetate buffer solution with the pH value of 4.4, stirring at 10 ℃ until the template is completely dissolved, adding 4.56g (0.04mol) of trimethylpentane into the solution, stirring at 10 ℃ for 8h, adding 1.83g (0.012mol) of tetramethoxysilane into the solution, stirring at 10 ℃ for 30h, transferring the solution into an agate-lined reaction kettle, oven-crystallizing at 80 ℃ for 20h, filtering, washing with deionized water for 6 times, and suction-filtering to obtain a filter cake A21 of the mesoporous molecular sieve material with the one-dimensional hollow spherical pore structure.

Adding hexadecyl trimethyl ammonium bromide and ethyl orthosilicate into an ammonia water solution with the concentration of 25 weight percent at 50 ℃, and adding deionized water, wherein the adding amount of the ethyl orthosilicate is 1g, and the mol ratio of ammonia to water in the ethyl orthosilicate, the hexadecyl trimethyl ammonium bromide and the ammonia water is 1: 0.5: 1.5: 180, stirring for 7 hours at the temperature of 50 ℃, then carrying out suction filtration on the solution and washing the solution with distilled water for four times to obtain a filter cake A22 of the mesoporous molecular sieve material with the hexagonal pore structure;

mixing 20 wt% of water glass, 12 wt% of sulfuric acid solution and glycerol in a weight ratio of 3: 2: 1, and then the reaction mixture was subjected to a contact reaction at 20 ℃ for 3 hours, followed by adjusting the pH to 4 with sulfuric acid having a concentration of 98% by weight, and then the resulting reaction mass was subjected to suction filtration and washed with distilled water until the sodium ion content was 0.02% by weight, to obtain a silica gel cake B2.

6.7g of the filter cake A21, 3.3g of the filter cake A22 and 15g of the filter cake B2 are placed into a 100mL ball milling tank together, wherein the ball milling tank is made of agate, grinding balls are made of agate, the diameter of the grinding balls is 3mm, the number of the grinding balls is 1, and the rotating speed is 500 r/min. And sealing the ball milling tank, and carrying out first ball milling in the ball milling tank at the temperature of 35 ℃ for 20 hours. The resulting first ball-milled slurry was mixed with 87.5g of water at 35 ℃ for slurrying, followed by second ball milling at 25 ℃ for 10 hours. And (3) spray-drying the obtained second ball-milling slurry at the rotation speed of 13000r/min at the temperature of 150 ℃, then screening by adopting a cyclone separation technology, calcining the screened product in a muffle furnace at the temperature of 600 ℃ for 15h, and removing P123 (template) to obtain the spherical porous mesoporous composite material C2.

The pore structure parameters of the spherical porous mesoporous composite material C2 are shown in table 2 below.

TABLE 2

*: the first most probable aperture, the second most probable aperture and the third most probable aperture are separated by commas.

(2) Preparation of the catalyst

0.1g of magnesium chloride and 0.2g of titanium tetrachloride were dissolved in 10mL of a composite solvent of tetrahydrofuran and isopropanol (the volume ratio of tetrahydrofuran to isopropanol was 1: 1.5) to form a catalyst mother liquor. 1g of spherical porous mesoporous composite material C2 was added to the mother liquor at 60 ℃ for immersion for 1h, then filtered, and washed with n-hexane for 4 times, dried at 75 ℃ and ground to obtain catalyst D2.

As a result of X-ray fluorescence analysis, the catalyst D1 obtained in this example had a magnesium element content of 6.9 wt% and a titanium element content of 1.1 wt%, calculated as elements.

(3) Ethylene polymerization

In a 2L stainless steel high pressure polymerization reactor, nitrogen and ethylene were each replaced three times, then 200mL of hexane was added, the reactor was warmed to 75 ℃ and 900mL of hexane was added, 2mL of a 1mol/L Triethylaluminum (TEA) solution in hexane was added with the addition of hexane, then 0.1g of catalyst component D2 was added, ethylene gas was introduced, the pressure was raised to 1MPa and maintained at 1MPa, and after 1.5 hours of reaction at 75 ℃ the reaction solution was separated by suction filtration to obtain polyethylene pellet powder. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

Example 3

(1) Preparation of spherical porous mesoporous composite material

Adding 1g (0.00017mol) of template P123 and 3.13g (0.068mol) of ethanol into 28mL of acetic acid and sodium acetate buffer solution with the pH value of 4.4, stirring at 20 ℃ until the template is completely dissolved, adding 7.75g (0.068mol) of trimethylpentane into the solution, stirring at 20 ℃ for 8h, adding 3.8g (0.025mol) of tetramethoxysilane into the solution, stirring at 20 ℃ for 10h, transferring the solution into an agate-lined reaction kettle, oven-crystallizing at 40 ℃ for 30h, filtering, washing with deionized water for 6 times, and carrying out suction filtration to obtain a filter cake A31 of the mesoporous molecular sieve material with the one-dimensional hollow pore structure.

Adding hexadecyl trimethyl ammonium bromide and ethyl orthosilicate into an ammonia water solution with the concentration of 25 weight percent at 90 ℃, and adding deionized water, wherein the adding amount of the ethyl orthosilicate is 1g, and the mol ratio of ammonia to water in the ethyl orthosilicate, the hexadecyl trimethyl ammonium bromide and the ammonia water is 1: 0.2: 3.5: 120 and stirred at a temperature of 90 ℃ for 3 hours, then the solution is filtered by suction and washed four times with distilled water, obtaining a filter cake a32 of the mesoporous molecular sieve material with a hexagonal pore structure.

Mixing 10 wt% of water glass, 12 wt% of sulfuric acid solution and ethylene glycol in a weight ratio of 6: 3: 1, then brought into contact with sulfuric acid having a concentration of 98% by weight to a pH of 2, and the resulting reaction mass was filtered with suction and washed with distilled water to a sodium ion content of 0.02% by weight to give a silica gel cake B3.

And (3) putting 7g of the prepared filter cake A31, 14g of the prepared filter cake A32 and 10g of the prepared filter cake B3 into a 100mL ball milling tank together, wherein the ball milling tank is made of agate, the grinding balls are made of agate, the diameter of each grinding ball is 3mm, the number of the grinding balls is 1, and the rotating speed is 300 r/min. And sealing the ball milling tank, and carrying out first ball milling in the ball milling tank at the temperature of 50 ℃ for 10 hours. The obtained first ball-milled slurry was mixed with 15g of water at 50 ℃ for pulping, followed by second ball-milling at 40 ℃ for 5 hours. And (3) spray-drying the obtained second ball-milling slurry at 250 ℃ at the rotating speed of 11000r/min, then screening by adopting a cyclone separation technology, calcining the screened product in a muffle furnace at 300 ℃ for 24h, and removing P123 (template) to obtain the spherical porous mesoporous composite material C3.

The pore structure parameters of the obtained spherical porous mesoporous composite material C3 are shown in table 3 below.

TABLE 3

(2) Preparation of the catalyst

0.2g of magnesium chloride and 0.1g of titanium tetrachloride were dissolved in 10mL of a composite solvent of tetrahydrofuran and isopropanol (the volume ratio of tetrahydrofuran to isopropanol was 1: 1) to form a catalyst mother liquor. 1g of spherical porous mesoporous composite material C3 was added to the mother liquor at 40 ℃ for immersion for 3h, then filtered, and washed with n-hexane for 4 times, dried at 75 ℃ and ground to obtain catalyst D3.

As a result of X-ray fluorescence analysis, the catalyst D1 obtained in this example had a magnesium element content of 6.6 wt% and a titanium element content of 0.8 wt%, calculated as elements.

(3) Ethylene polymerization

In a 2L stainless steel high pressure polymerization reactor, nitrogen and ethylene were each replaced three times, then 200mL of hexane was added, the reactor was warmed to 85 ℃ and 700mL of hexane was added, 2mL of a 1mol/L Triethylaluminum (TEA) solution in hexane was added with the addition of hexane, then 1g of catalyst component D3 was added, ethylene gas was introduced, the pressure was raised to 1MPa and maintained at 1MPa, and after reacting at 85 ℃ for 2 hours, separation by suction filtration, a polyethylene pellet powder was obtained. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

Example 4

A spherical porous mesoporous composite and a supported catalyst were prepared in the same manner as in example 1, except that glycerol was not added in the preparation of the filter cake of silica gel, to obtain a spherical porous mesoporous composite C4 and a catalyst D4.

The pore structure parameters of the spherical porous mesoporous composite material C4 are shown in table 4 below.

TABLE 4

The catalyst D4 according to this example contained 7.5 wt% of magnesium and 0.8 wt% of titanium, calculated as elements, by X-ray fluorescence analysis.

(3) Ethylene polymerization

Polymerization of ethylene was carried out in accordance with the procedure of Experimental example 1, except that the same parts by weight of the catalyst D4 prepared in example 4 was used in place of the catalyst D1 prepared in example 1. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16Crushing rate and catalyst efficiencyThe ratios are listed in table 8.

Comparative example 1

This comparative example serves to illustrate a reference ethylene polymerization process and polyethylene

Commercially available ES955 silica Gel (GRACE) was calcined under nitrogen at 400 deg.C for 10h to remove hydroxyl groups and residual moisture, thereby obtaining heat-activated ES955 silica gel.

A catalyst was prepared according to the procedure of step (2) of example 1, except that the same parts by weight of the above-mentioned activated ES955 silica gel was used in place of the spherical porous mesoporous composite C1, thereby preparing a comparative catalyst DD 1.

(3) Ethylene polymerization

Polymerization of ethylene was carried out in accordance with the procedure of Experimental example 1, except that the catalyst D1 prepared in example 1 was replaced with the same parts by weight of comparative catalyst DD1, respectively. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

Comparative example 2

The spherical porous mesoporous composite and the supported catalyst were prepared according to the method of example 1. Except that only the first ball milling was performed, and the second ball milling was not performed. Specifically, 5g of the filter cake A11 prepared above, 5g of the filter cake A12 and 10g of the filter cake B1 were put together in a 100mL ball mill pot. And sealing the ball milling tank, and carrying out first ball milling in the ball milling tank at the temperature of 25 ℃ for 5 hours. The first ball-milled slurry obtained was mixed with 40g of water at 25 ℃ for slurrying, and the slurry obtained was spray-dried at 200 ℃ at 12000 r/min. The spherical porous mesoporous composite material DC2 and the supported catalyst DD2 are prepared.

The pore structure parameters of the spherical porous mesoporous composite material DC2 are shown in table 5 below.

TABLE 5

According to X fluorescence analysis, in the catalyst DD2, the content of magnesium element is 6.1 wt% and the content of titanium element is 0.7 wt% calculated by element.

(3) Ethylene polymerization

Polymerization of ethylene was carried out in accordance with the procedure of experimental example 1 except that the catalyst D1 prepared in example 1 was replaced with the same parts by weight of the catalyst DD2, respectively. The Bulk Density (BD) of the polyethylene pellet powder obtained, the melt index MI2.16, the crushing rate and the efficiency of the catalyst are shown in Table 8.

Comparative example 3

The spherical porous mesoporous composite and the supported catalyst were prepared according to the method of example 1. The difference is that the screening is not carried out by adopting a cyclone separation technology, specifically, the obtained second ball-milling slurry is subjected to spray drying at the temperature of 200 ℃ and the rotating speed of 12000r/min, then a product obtained after the spray drying is calcined for 10 hours at the temperature of 550 ℃ in a muffle furnace, and P123 (template) is removed, so that the spherical porous mesoporous composite materials DC3 and DD3 are obtained.

The pore structure parameters of the spherical porous mesoporous composite material DC3 are shown in table 6 below.

TABLE 6

According to X fluorescence analysis, in the catalyst DD3, the content of magnesium element is 6.0 wt% and the content of titanium element is 1.1 wt% calculated by element.

(3) Ethylene polymerization

Polymerization of ethylene was conducted in accordance with the procedures of Experimental example 1, except that the same parts by weight of catalyst DD3 was used instead of conductingCatalyst D1 prepared in example 1. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

Comparative example 4

The spherical porous mesoporous composite and the supported catalyst were prepared according to the method of example 1. The difference is that only the first ball milling is carried out, the second ball milling is not carried out, and the cyclone separation technology is not adopted for screening. Specifically, 5g of the filter cake A11 prepared above, 5g of the filter cake A12 and 10g of the filter cake B1 were put together in a 100mL ball mill pot. And sealing the ball milling tank, and carrying out first ball milling in the ball milling tank at the temperature of 25 ℃ for 5 hours. And mixing the obtained first ball-milling slurry with 40g of water at 25 ℃ for pulping, spray-drying the obtained slurry at 200 ℃ at the rotating speed of 12000r/min, calcining the spray-dried product in a muffle furnace at 550 ℃ for 10h, and removing P123 (template) to obtain the spherical porous mesoporous composite materials DC4 and DD 4.

The pore structure parameters of the spherical porous mesoporous composite material DC2 are shown in table 7 below.

TABLE 7

According to X fluorescence analysis, in the catalyst DD3, the content of magnesium element is 5.6 wt% and the content of titanium element is 0.9 wt% calculated by element.

(3) Ethylene polymerization

Polymerization of ethylene was carried out in accordance with the procedure of experimental example 1 except that the catalyst D1 prepared in example 1 was replaced with the same parts by weight of the catalyst DD4, respectively. Bulk Density (BD) and melt index MI of the obtained polyethylene granular powder_2.16The pulverization rates and the catalyst efficiencies are shown in Table 8.

TABLE 8

As can be seen from the results of comparing the above experimental examples 1 to 4 with the experimental comparative examples 1 to 4, when the spherical porous mesoporous composite material and the supported catalyst of the present invention are used in an ethylene polymerization reaction, the catalyst has high catalytic activity, and a polyethylene product having low bulk density and melt index and being not easily broken can be obtained, specifically, the prepared polyethylene product has a bulk density of 0.5g/mL or less, a melt index of 0.5g/10min or less, and a pulverization rate of less than 3 wt%. The polyethylene products which are not obtained by the method of the invention have the crushing rate of more than 5 weight percent.

The preferred embodiments of the present invention have been described in detail, however, the present invention is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present invention within the technical idea of the present invention, and these simple modifications are within the protective scope of the present invention.

It should be noted that the various features described in the above embodiments may be combined in any suitable manner without departing from the scope of the invention. The invention is not described in detail in order to avoid unnecessary repetition.

In addition, any combination of the various embodiments of the present invention is also possible, and the same should be considered as the disclosure of the present invention as long as it does not depart from the spirit of the present invention.

Claims

1. A process for the polymerization of ethylene, the process comprising: polymerizing ethylene in the presence of a catalyst under a polymerization condition, wherein the catalyst comprises a spherical porous mesoporous composite material and a magnesium salt and/or a titanium salt loaded on the spherical porous mesoporous composite material, the spherical porous mesoporous composite material comprises a mesoporous molecular sieve material with a one-dimensional through pore channel structure and a mesoporous molecular sieve material with a hexagonal pore channel structure, the average particle diameter of the spherical porous mesoporous composite material is 21-29 microns, the specific surface area is 200-650 square meters per gram, the pore volume is 0.5-1.8 milliliters per gram, the pore diameters are in a trimodal distribution, the trimodal corresponds to a first most probable pore diameter, a second most probable pore diameter and a third most probable pore diameter respectively, the first most probable pore diameter is 1-10 nanometers, and the second most probable pore diameter is 20-35 nanometers, the third mode pore diameter is 40-50 nanometers;

the spherical porous mesoporous composite material is prepared by the following steps:

(4) mixing the component a1, the component a2 and the component b, performing first ball milling, mixing the obtained first ball milling slurry with water for pulping, performing second ball milling to obtain second ball milling slurry, performing spray drying on the second ball milling slurry, and screening by adopting a cyclone separation technology.

2. The method according to claim 1, wherein the spherical porous mesoporous composite material is contained in an amount of 90 to 99 wt%, and the sum of the contents of the magnesium salt and the titanium salt, calculated as magnesium element and titanium element, respectively, is 1 to 10 wt%, based on the total weight of the catalyst.

3. The method of claim 1, wherein the catalyst is prepared by contacting the spherical porous mesoporous composite with a mother liquor comprising a magnesium salt and/or a titanium salt in the presence of an inert gas.

4. The method of claim 3, wherein the conditions of the contacting comprise: the temperature is 25-100 ℃ and the time is 0.1-5 h.

5. The method according to any one of claims 1 to 4, wherein, in step (4), the component b is used in an amount of 1 to 200 parts by weight, relative to 100 parts by weight of the total amount of the component a1 and the component a 2.

6. The method as claimed in claim 5, wherein, in the step (4), the component b is used in an amount of 20-180 parts by weight, relative to 100 parts by weight of the total amount of the component a1 and the component a 2.

7. The method as claimed in claim 5, wherein, in the step (4), the component b is used in an amount of 50-150 parts by weight, relative to 100 parts by weight of the total amount of the component a1 and the component a 2.

8. The process according to any one of claims 1 to 4, wherein the weight ratio of component a1 to component a2 is 1: 0.1-10.

9. The method of claim 8, wherein the weight ratio of component a1 to component a2 is 1: 0.5-2.

10. The method of claim 1, wherein, in step (1), the process of preparing a filter cake of mesoporous molecular sieve material having a one-dimensional through-channel structure comprises: the template agent, a silicon source, ethanol, trimethylpentane and an acid agent are subjected to first mixing contact, and a mixture obtained by the first mixing contact is crystallized and filtered.

11. The method of claim 10, wherein the templating agent is a triblock copolymer polyethylene glycol-polyglycerol-polyethylene glycol; the silicon source is tetramethoxysilane; the acid agent is acetic acid and sodium acetate buffer solution with pH value of 1-6.

12. The method of claim 10 or 11, wherein the molar ratio of the templating agent, ethanol, trimethylpentane, and silicon source is 1: 100-500: 200-500: 50-200.

13. The method of claim 12, wherein the mole ratio of the templating agent, ethanol, trimethylpentane, and silicon source is 1: 180-400: 250-400: 70-150.

14. The method of claim 10, wherein the conditions of the first mixing contact comprise: the temperature is 10-60 ℃, the time is 10-72 hours, and the pH value is 1-7; the conditions for crystallization of the mixture obtained by the first mixing contact include: the temperature is 30-150 ℃ and the time is 10-72 hours.

15. The method of claim 1, wherein, in step (2), the process of preparing a filter cake of mesoporous molecular sieve material having a hexagonal pore structure comprises: and (3) carrying out second mixing contact on ethyl orthosilicate, hexadecyl trimethyl ammonium bromide and ammonia, and filtering a mixture obtained by the second mixing contact.

16. The method of claim 15, wherein the molar ratio of ethyl orthosilicate, cetyltrimethylammonium bromide, and ammonia is 1: 0.1-1: 0.1-5.

17. The method of claim 16, wherein the molar ratio of ethyl orthosilicate, cetyltrimethylammonium bromide, and ammonia is 1: 0.2-0.5: 1.5-3.5.

18. The method of any one of claims 15-17, wherein the conditions of the second mixing contact comprise: the temperature is 25-100 ℃ and the time is 2-8 hours.

19. The method of claim 1, wherein, in the step (3), the process of preparing the filter cake of silica gel comprises: and carrying out third mixing contact on the water glass, the polyhydric alcohol and the inorganic acid, and filtering a mixture obtained by the third mixing contact.

20. The method of claim 19, wherein the conditions of the third mixed contacting comprise: the temperature is 10-60 deg.C, the time is 1-5 hr, and the pH value is 2-4.

21. The method of claim 19 or 20, wherein the weight ratio of the water glass, the inorganic acid and the polyol is 1-8: 0.1-5: 1; the inorganic acid is one or more of sulfuric acid, nitric acid and hydrochloric acid; the polyalcohol is glycerol and/or ethylene glycol.

22. The method of any one of claims 1 to 4, wherein in step (4), the conditions of the first ball mill and the second ball mill are the same or different, and each of the conditions of the first ball mill and the second ball mill independently comprises: the rotation speed of the grinding ball is 200-800r/min, the temperature in the ball milling tank is 15-100 ℃, and the ball milling time is 0.1-100 hours.

23. The method of claim 22, wherein the first ball-milled slurry is used in an amount of 1: 0.1-5 ℃, and the temperature for mixing the first ball-milling slurry and water for pulping is 25-60 ℃.

24. The method of claim 1, wherein the conditions of the spray drying comprise: the temperature is 150-600 ℃, and the rotating speed is 10000-15000 r/min.

25. The method of claim 22, wherein the step of screening the second ball-milled slurry using a cyclone technique after spray drying comprises: and carrying out spray drying on the second ball-milling slurry, and carrying out cyclone separation on the discharged gas containing the powder particles so as to collect the powder particles.

26. The process according to any one of claims 1 to 4, wherein component a1 is a filter cake of a mesoporous molecular sieve material having a one-dimensional through-channel structure, component a2 is a filter cake of a mesoporous molecular sieve material having a hexagonal channel structure, and component b is a filter cake of silica gel; the method further comprises the following steps: after the spray drying process of step (4), the templating agent is removed from the powder particles collected by cyclone separation.

27. The method of claim 26, wherein the conditions to remove the templating agent comprise: the temperature is 90-600 ℃, and the time is 10-80 hours.

28. The process of any one of claims 1-4, wherein the polymerization reaction is carried out in the presence of an inert gas under conditions comprising: the temperature is 10-100 ℃, the time is 0.5-5h, and the pressure is 0.1-2 MPa.

29. A polyethylene produced by the process of any one of claims 1 to 28.