CN102718898A - Olefin polymerization method - Google Patents
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- CN102718898A CN102718898A CN2011100803143A CN201110080314A CN102718898A CN 102718898 A CN102718898 A CN 102718898A CN 2011100803143 A CN2011100803143 A CN 2011100803143A CN 201110080314 A CN201110080314 A CN 201110080314A CN 102718898 A CN102718898 A CN 102718898A
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Abstract
The invention provides an olefin polymerization method, characterized by contacting one or more olefins with a loaded metallocene catalyst under olefin polymerization conditions, wherein the loaded metallocene catalyst comprises a carrier and a metallocene compound loaded on the carrier, and the carrier is rodlike macroporous silica. According to the loaded metallocene catalyst of the invention, the metallocene compound has a sandwich structure and has substituents on cyclopentadienyl, wherein the rodlike macroporous silica has highly-ordered large aperture (11-12 nanometers) and pore volume, good mechanical strength and good macro-molecule catalytic and adsorption properties, thus high catalytic activity is achieved.
Description
Technical field
The present invention relates to a kind of olefine polymerizing process.
Background technology
The Application and Development of metallocene catalyst is after traditional Ziegler-Natta catalyst, the another important breakthrough in olefin polymerization catalysis field.Because to reach the required MAO of high reactivity (MAO) consumption big for the homogeneous phase metallocene catalyst, production cost is high, and the polymkeric substance that obtains do not have particle shape, can't on widely used slurry process or gas phase polymerization technology, use.And the activity of metallocene catalyst is very high, and it is very fast in polymerization process, to be easy to take place local polymerization velocity, and then causes implode.
The effective way that addresses the above problem is carried out the load processing to the solubility metallocene catalyst exactly.At present, relevant metallocene catalyst load research report is very many, wherein with SiO
2Maximum for the report research of carrier, for example: CN1095474C, CN1049439C, CN1157419C, US4808561, US5026797, US5763543 and US5661098 all disclose with SiO
2Carried metallocene catalyst for carrier.Yet, for furtheing investigate new support/catalyst/co-catalyst system, be necessary to attempt different carriers, to promote further developing of carried catalyst and polyolefin industry.
Molecular sieve is to have the evenly regular one dimension or the material of solid netted sieve aperture, and surfactivity is higher, absorption property good, have tangible molecule shape selectivity ability, and its allows the monomer of certain size and the polymkeric substance of formation thereof to insert in the duct of molecular sieve.And because molecular sieve has nano pore, monomeric inserted mode is different with freeboard with propagation process in the polymerization process, and double-basis terminated chance has been reduced in limited space to a certain extent, makes polyreaction show the characteristic of " living polymerization ".
Olefin polymerization catalysis is carried on molecular sieve, has following advantage:
(1) molecular sieve of synthetic does not contain the impurity that is prone to make polymer degradation, with the ageing resistance that improves polyolefine material;
(2) the molecular sieve nano pore has the dual-use function of carrier and reactor drum, and catalyst cupport efficient is high, and polymerization process is controlled easily, and can in the skeleton of polymerization reactor, key in the active site, accelerates reaction process, improves productive rate;
(3) insertion has three-dimensional selection effect with polyreaction to monomer, can improve polyolefinic molecular weight and fusing point.
This shows that the olefin coordination polymerization that appears as of molecular sieve carried olefin polymerization catalysis has been opened up a new field.
Compare with industrial silica gel, ordered mesoporous molecular sieve has bigger specific surface area, can handle bigger molecule or group, can make catalyzer bring into play its due catalytic activity well.The mesopore molecular sieve that aperture at present commonly used is the 5-7 nanometer is as support of the catalyst.Therefore, how to obtain the carried metallocene catalyst of high catalytic efficiency (, and then carry out olefinic polymerization efficiently and remain a technical problem that needs to be resolved hurrily.
Summary of the invention
The catalytic efficiency (of carried metallocene catalyst that the objective of the invention is to overcome prior art is still lower, causes adopting the not high problem of efficient of the olefinic polyreaction of carried metallocene catalyst, and a kind of olefine polymerizing process efficiently is provided.
Contriver of the present invention finds; Through adopting mesoporous material that the aperture suitably increases (is the 11-20 nanometer like the aperture) as carrier, the activity of such catalysts of acquisition can obviously improve, and traces it to its cause; Possibly be that to adopt the aperture be that the mesopore molecular sieve of 5-7 nanometer is during as carrier for existing catalyzer; Metallocene entering duct is easy to stop up in the loading process, causes the catalytic activity of catalyzer not give full play of, thereby causes the efficient of olefinic polymerization not high.In addition, when carrying out vinyl polymerization, to get into abundant duct inner because load metallocene mainly is load, during polymerization inductive phase longer, the implode phenomenon of polymerization reaction kettle can not appear impairing.
The invention provides a kind of olefine polymerizing process, this method is included under the olefinic polymerization condition, and one or more alkene are contacted with carried metallocene catalyst; It is characterized in that; Said carried metallocene catalyst comprises carrier and loads on metallocene compound and the alkylaluminoxane on the said carrier, and said carrier is bar-shaped macropore mesoporous silicon oxide, and the most probable aperture of said bar-shaped macropore mesoporous silicon oxide is the 11-20 nanometer; Said metallocene compound has the structure shown in the formula 1
Wherein, R
1, R
2, R
3, R
4, R
5, R
1', R
2', R
3', R
4' and R
5' be hydrogen or C independently of one another
1-C
5Alkyl, and R
1, R
2, R
3, R
4And R
5In at least one be C
1-C
5Alkyl, R
1', R
2', R
3', R
4' and R
5' at least one be C
1-C
5Alkyl, M is a kind of in titanium, zirconium and the hafnium, X is a halogen.
According to olefine polymerizing process of the present invention; Because metallocene compound has sandwich structure described in the catalyst system therefor; And have substituting group on the cyclopentadienyl moiety, carrier is the bar-shaped macropore mesoporous silicon oxide of 11-20 nanometer for the most probable aperture, so the catalytic activity of catalyzer obviously improves.
Particularly, according to olefine polymerizing process of the present invention, the ethylene homo catalytic efficiency (can reach 1887gPE/gcat.h (that is, 3.4 * 10
7GPE/mol Zrh), and under the identical situation of other conditions, the ethylene homo catalytic efficiency (during metallocene compound that industrial 955 silica gel loads have the structure shown in the formula 1 be merely 1300gPE/gcath (, 2.9 * 10
7GPE/mol Zrh).
Description of drawings
Fig. 1 is the x-ray diffraction pattern (a) of bar-shaped macropore meso-porous titanium dioxide silicon carrier KKSBA-15, X-coordinate unit be 2 θ (°), ordinate zou is an intensity;
Fig. 2 is the x-ray diffraction pattern (b) of carried metallocene catalyst KKSBA-15-BU, X-coordinate unit be 2 θ (°), ordinate zou is an intensity;
Fig. 3 and Fig. 4 are respectively the N of bar-shaped macropore meso-porous titanium dioxide silicon carrier KKSBA-15 (a) and carried metallocene catalyst KKSBA-15-BU (b)
2The adsorption desorption graphic representation, wherein, X-coordinate is a relative pressure, unit is p/p
0, ordinate zou is pore volume absorption, unit is cm
3/ gSTP;
Fig. 5 and Fig. 6 are respectively the graph of pore diameter distribution (b) of bar-shaped macropore meso-porous titanium dioxide silicon carrier KKSBA-15 (a) and carried metallocene catalyst KKSBA-15-BU, and wherein, X-coordinate is the aperture, and unit is nm, and ordinate zou is dv/dlog, and unit is cm
3/ g;
A is the stereoscan photograph of bar-shaped macropore meso-porous titanium dioxide silicon carrier KKSBA-15 among Fig. 7, the stereoscan photograph of b carried metallocene catalyst KKSBA-15-BU.
Embodiment
The invention provides a kind of olefine polymerizing process, this method is included under the olefinic polymerization condition, and one or more alkene are contacted with carried metallocene catalyst; Wherein, Said carried metallocene catalyst comprises carrier and loads on metallocene compound and the alkylaluminoxane on the said carrier, and said carrier is bar-shaped macropore Metaporous silicon dioxide material, and the most probable aperture of said bar-shaped macropore mesoporous silicon oxide is the 11-20 nanometer; Said metallocene compound has the structure shown in the formula 1
Wherein, R
1, R
2, R
3, R
4, R
5, R
1', R
2', R
3', R
4' and R
5' be hydrogen or C independently of one another
1-C
5Alkyl, and R
1, R
2, R
3, R
4And R
5In at least one be C
1-C
5Alkyl, R
1', R
2', R
3', R
4' and R
5' at least one be C
1-C
5Alkyl, M is a kind of in titanium, zirconium and the hafnium, X is a halogen.
According to the present invention, what the M in the formula 1 can be in titanium, zirconium and the hafnium is a kind of.M in the different metallocene compounds can be identical or different, and preferably, M is a zirconium.
According to the present invention, the X in the formula 1 is a halogen.What particularly, the X in the formula 1 can be in fluorine, chlorine, bromine and the iodine is a kind of.Preferably, the X in the formula 1 is a chlorine or bromine.X in the different metallocene compounds can be identical or different, and more preferably, the X in the formula 1 is a chlorine.
According to the present invention, in the formula 1, cyclopentadienyl moiety is the verivate that can form η 5 keys with central metal M and have the cyclopentadienyl of alkyl substituent.Preferably, the R on the cyclopentadienyl moiety in the formula 1
1, R
2, R
3, R
4, R
5, R
1', R
2', R
3', R
4' and R
5' be hydrogen or C independently of one another
1-C
5Alkyl, and R
1, R
2, R
3, R
4, R
5In at least one be C
1-C
5Alkyl, R
1', R
2', R
3', R
4' and R
5' at least one be C
1-C
5Alkyl.
Among the present invention, said C
1-C
5Alkyl can be in methyl, ethyl, n-propyl, sec.-propyl, normal-butyl, sec.-butyl, isobutyl-, the tertiary butyl, n-pentyl, isopentyl, tert-pentyl and the neo-pentyl one or more.
The specific examples that satisfies the cyclopentadienyl moiety of above-mentioned requirements comprises: methyl-cyclopentadienyl moiety, 1,2-dimethyl--cyclopentadienyl moiety, 1,3-dimethyl--cyclopentadienyl moiety, 1; 2,3-trimethylammonium-cyclopentadienyl moiety, 1,2; 5-trimethylammonium-cyclopentadienyl moiety, 1,2,3; 4-tetramethyl--cyclopentadienyl moiety, 1,2,3; 5-tetramethyl--cyclopentadienyl moiety, pentamethyl-cyclopentadienyl moiety, ethyl-cyclopentadienyl moiety, 1,2-diethylammonium-cyclopentadienyl moiety, 1,3-diethylammonium-cyclopentadienyl moiety, 1; 2; 4-triethyl-cyclopentadienyl moiety, 1,3,5-triethyl-cyclopentadienyl moiety, methyl-2-ethyl-cyclopentadienyl moiety, 1-methyl-3-ethyl-cyclopentadienyl moiety, n-propyl-cyclopentadienyl moiety, 1; 3-di-cyclopentadienyl moiety, 1-methyl-3-n-propyl-cyclopentadienyl moiety, 1; 3-di-isopropyl-cyclopentadienyl moiety, 1-methyl-3-sec.-propyl-cyclopentadienyl moiety, normal-butyl-cyclopentadienyl moiety, 1,3-di-n-butyl-cyclopentadienyl moiety, 1-methyl-3-normal-butyl-cyclopentadienyl moiety, sec.-butyl-cyclopentadienyl moiety, 1,3-two sec.-butyls-cyclopentadienyl moiety, 1-methyl-3-sec.-butyl-cyclopentadienyl moiety, 1-isobutyl--cyclopentadienyl moiety, 1; 3-diisobutyl-cyclopentadienyl moiety, 1-methyl 3-isobutyl--cyclopentadienyl moiety, the tertiary butyl-cyclopentadienyl moiety, 1; 3-di-t-butyl-cyclopentadienyl moiety, the 1-methyl 3-tertiary butyl-cyclopentadienyl moiety, n-pentyl-cyclopentadienyl moiety, 1,3-two n-pentyls-cyclopentadienyl moiety, 1-methyl-3-n-pentyl-cyclopentadienyl moiety, 1-isopentyl-cyclopentadienyl moiety, 1,3-diisoamyl-cyclopentadienyl moiety, 1-methyl-3-isopentyl-cyclopentadienyl moiety, 1-tert-pentyl-cyclopentadienyl moiety, 1; 3-two tert-pentyls-cyclopentadienyl moiety, 1-methyl-3-tert-pentyl-cyclopentadienyl moiety, neo-pentyl-cyclopentadienyl moiety, 1,3-di neo-pentyl-cyclopentadienyl moiety, 1-methyl-3-neo-pentyl-cyclopentadienyl moiety.
Preferably, the R in the formula 1
1, R
1' and be C independently of one another
1-C
5Alkyl, R
2, R
3, R
4, R
5, R
2', R
3', R
4' and R
5' be hydrogen.
The specific examples that satisfies the cyclopentadienyl moiety of above-mentioned requirements comprises: methyl-cyclopentadienyl moiety, ethyl-cyclopentadienyl moiety, n-propyl-cyclopentadienyl moiety, sec.-propyl-cyclopentadienyl moiety, normal-butyl-cyclopentadienyl moiety, sec.-butyl-cyclopentadienyl moiety, isobutyl--cyclopentadienyl moiety, the tertiary butyl-cyclopentadienyl moiety, n-pentyl-cyclopentadienyl moiety, isopentyl-cyclopentadienyl moiety, tert-pentyl-cyclopentadienyl moiety, neo-pentyl-cyclopentadienyl moiety.
More preferably, R
1And R
1' be C
4Alkyl, R
2, R
3, R
4, R
5, R
2', R
3', R
4' and R
5' be hydrogen.Particularly, said cyclopentadienyl moiety is n-butyl cyclopentadienyl, sec.-butyl cyclopentadienyl moiety, isobutyl-cyclopentadienyl moiety, tertiary butyl cyclopentadienyl moiety.
According to the present invention, said alkylaluminoxane can be metallocene catalyst field various alkylaluminoxanes commonly used.Usually, the alkyl in the said alkylaluminoxane is aforesaid C
1-C
5Alkyl.Preferably, said alkylaluminoxane is a MAO.
Contriver of the present invention finds in research process, the R in formula 1
1And R
1' be normal-butyl, M is a zirconium, X is a chlorine; Be that said metallocene compound is two (n-butyl cyclopentadienyl) zirconium dichlorides; And when alkylaluminoxane is MAO, when said carried metallocene catalyst is used for the polyreaction of catalyzed alkene, demonstrate excellent catalytic activity.
According to the present invention, the metallocene compound and the amount of alkylaluminoxane that load on the said carrier can change within a large range.Contriver of the present invention finds, is benchmark with the total amount of said carried metallocene catalyst, and the total amount of said metallocene compound and alkylaluminoxane is 20-50 weight %, and the content of said carrier is 50-80 weight %.Under the preferable case, be benchmark with the total amount of said carried metallocene catalyst, the total amount of said metallocene compound and alkylaluminoxane is 30-40 weight %, and the content of said carrier is 60-70 weight %.Further under the preferable case, be benchmark with the total amount of said carried metallocene catalyst, the total amount of said metallocene compound and alkylaluminoxane is 33-34 weight %, and the content of said carrier is 66-67 weight %.
According to the present invention, the said alkylaluminoxane and the ratio between the metallocene compound that load on the said carrier can be the known ratio of the technician of field of olefin polymerisation.Preferably, the mol ratio of the M in aluminium in the said alkylaluminoxane and the said metallocene compound can be 50-200 for the mol ratio of M: 1, be preferably 80-120: and 1,90-110 more preferably: 1, most preferably be 100: 1.
According to carried metallocene catalyst of the present invention, said metallocene compound has sandwich structure, and has substituting group on the cyclopentadienyl moiety; According to carried metallocene catalyst of the present invention, wherein, the length of bar-shaped carrier is the 2-20 micron; Length-to-diameter ratio is 2-8; Specific surface area is the 300-600 meters squared per gram, and pore volume is 0.3-1.5 milliliter/gram, and the most probable aperture is the 11-20 nanometer;
Under the preferable case, the length of bar-shaped carrier is the 3-15 micron, and length-to-diameter ratio is 3-7, and specific surface area is the 300-500 meters squared per gram, and pore volume is 0.5-1.2 milliliter/gram, and the most probable aperture is the 11-15 nanometer;
Further under the preferable case, the length of bar-shaped carrier is the 3-9 micron, and length-to-diameter ratio is the 4-6 micron, and specific surface area is the 300-400 meters squared per gram, and pore volume is 0.8-1.2 milliliter/gram, and the most probable aperture is the 11-12 nanometer;
Under the most preferred case, the length of bar-shaped carrier is 4 microns, and length-to-diameter ratio is 5, and specific surface area is 351 meters squared per gram, and pore volume is 1.0 a milliliters/gram, and the most probable aperture is 12 nanometers.
Said bar-shaped macropore mesoporous silicon oxide can prepare through the method that may further comprise the steps:
(1) template, water and HCl are stirred to dissolving under 25-60 ℃ of temperature;
(2) under 25-60 ℃ of temperature, stir more than 0.2 hour step (1) gained solution and tetraethoxy;
(3) with step (2) products therefrom crystallization under crystallization condition;
(4) step (3) gained crystallization product is used the alcoholic solvent contact of carbonatoms as 1-4, with removed template method;
Said template is polyoxyethylene-polyoxytrimethylene-polyoxyethylene triblock copolymer.
Said crystallization condition comprises that crystallization temperature is 90-180 ℃, and crystallization time is 10-40 hour.
Said crystallization product and carbonatoms are that the condition that the alcoholic solvent of 1-4 contacts comprises that temperature is 90-120 ℃, and the time is 10-40 hour.
Said crystallization product and carbonatoms are that the weight ratio of the alcoholic solvent of 1-4 is 1: 100-300.
Said carbonatoms is that the alcoholic solvent of 1-4 is an ethanol.
Count polyoxyethylene-polyoxytrimethylene-polyoxyethylene: water: hydrogenchloride=1: 9000-15000: 100-500, preferred 1: 10000: 290 in molar ratio.Wherein, the mole number of polyoxyethylene-polyoxytrimethylene-polyoxyethylene calculates according to the molecular-weight average of polyoxyethylene-polyoxytrimethylene-polyoxyethylene.
According to the present invention, said carried metallocene catalyst can be through under protection of inert gas, successively load alkylaluminoxane and metallocene compound and obtain on carrier.The content of alkylaluminoxane and metallocene compound satisfies the described requirement of preamble and gets final product in the carried metallocene catalyst that said alkylaluminoxane and the metallocene compound charge capacity on said carrier make to obtain.
According to the present invention, the kind of said alkylaluminoxane and metallocene compound is described in detail at preamble, repeats no more here.
Can adopt the method for well known to a person skilled in the art that alkylaluminoxane and metallocene compound are loaded on the said carrier.Preferably, successively the method at load alkylaluminoxane and metallocene compound on the carrier comprises: under protection of inert gas, said carrier is contacted with first solution, said first solution contains the said alkylaluminoxane and first solvent; The carrier that has removed said first solvent is contacted with second solution, and said second solution contains the said metallocene compound and second solvent, and removes second solvent.Said first solvent and second solvent can be identical or different, preferably are toluene.
Under the preferable case, count in molar ratio, carrier: toluene: the amount ratio of alkylaluminoxane is 1: 10-100: 0.1-2.
Under the preferable case, count in molar ratio, carrier: toluene: the amount ratio of metallocene compound is 1: 20-150: 2 * 10
-3-19 * 10
-3
Wherein, the mole number of alkylaluminoxane is in RAlO, and wherein R is an alkyl, and for example the mole number of MAO is with CH
3AlO (promptly 58) meter, the mole number of carrier is in silicon-dioxide.
The method that the present invention contacts with second solution for the carrier that said carrier is contacted and will remove said first solvent with first solution is not special to be limited, can be for well known to a person skilled in the art the whole bag of tricks, for example: dipping, spraying.The method of employing dipping can be so that solution gets in the duct on the carrier more fully, and therefore, the present invention is preferably flooded.
With not special qualification of condition that the carrier and first solution contact with second solution, for example: carrier can comprise with the condition that said first solution contacts: the time is 1-10 hour, and temperature is 25-80 ℃; The said carrier that has removed toluene can be comprised with the condition that said second solution contacts: the time is 0.3-2 hour, and temperature is 25-80 ℃.
According to the present invention, toluene preferably adopts the method that well known to a person skilled in the art to make with extra care before use, for example: can be through toluene be made with extra care on sodium in backflow 24-48 hour, with remove desolvate in impurity such as water.
According to the present invention; Also preferably before said alkylaluminoxane of load and said metallocene compound; Under protection of inert gas, said carrier was heated 7-10 hour under 300-900 ℃ temperature, (for example: water) with the volatile matter that contains in the hydroxyl of removing carrier surface and the carrier.Preferably; Be included in according to the method for the invention before said alkylaluminoxane of load and the said metallocene compound, under protection of inert gas, said carrier heated 9-10 hour under 350-450 ℃ temperature; More preferably, under 400 ℃ temperature, heated 10 hours.
According to the present invention, chemically interactive all gases can be for not taking place with carrier, alkylaluminoxane, metallocene compound in said rare gas element.For example, said rare gas element can be nitrogen, argon gas.
According to the present invention; The feasible total amount with said carried metallocene catalyst of said alkylaluminoxane and the metallocene compound charge capacity on said carrier is a benchmark; The total amount of said metallocene compound and alkylaluminoxane can be 20-50 weight %; More preferably 30-40 weight % further is preferably 33-34 weight %; The content of said carrier can be 50-80 weight %; More preferably 60-70 weight % further is preferably 66-67 weight %; The mol ratio of M in aluminium in the said alkylaluminoxane and the said metallocene compound can be 50-200: 1 is preferably 80-120: 1, and 90-110 more preferably: 1, most preferably be 100: 1.A preferred embodiment of the invention, the preparation method of said carried metallocene catalyst comprises:
The 1st step; With triblock copolymer polyoxyethylene-polyoxytrimethylene-polyoxyethylene as template; Join in the aqueous hydrochloric acid, by mole feed ratio, triblock copolymer polyoxyethylene-polyoxytrimethylene-polyoxyethylene: water: hydrogenchloride=1: 9000-15000: 100-500; Preferred 1: 10000: 290, under 25 ℃ of-60 ℃ of temperature, be stirred to dissolving;
The 2nd step added tetraethoxy in a last step gained solution, under 25 ℃ of-60 ℃ of temperature, stir more than 25 minutes, preferably stirred 24 hours down at 40 ℃;
The 3rd step, will go up step gained solution and place closed reaction vessel, crystallization is 10 hours-40 hours under 90 ℃ of-180 ℃ of temperature, preferably 150 ℃ of following crystallization 24 hours;
In the 4th step,, obtain the former powder of bar-shaped macropore mesoporous silicon oxide with the filtration of crystallization after product, washing, drying;
The 5th step, the former powder of the bar-shaped macropore mesoporous silicon oxide of gained was washed 10 hours-40 hours under 90 ℃ of-120 ℃ of temperature with ethanol, preferably washed 10 hours down at 100 ℃, removed template method obtains bar-shaped macropore mesoporous silicon oxide;
In the 6th step, the thermal activation step will go up step gained bar-shaped macropore mesoporous silicon oxide under nitrogen protection, in 300-900 ℃ of calcining 7-10 hour, preferably 400 ℃ of calcinings 10 hours down, obtain the bar-shaped macropore mesoporous silicon oxide after the thermal activation;
The 7th step was transferred to the bar-shaped macropore mesoporous silicon oxide after the thermal activation in the reactor drum after nitrogen is fully replaced, and added toluene and alkylaluminoxane; Count in molar ratio, bar-shaped macropore mesoporous silicon oxide (in silicon-dioxide): toluene: the amount ratio of alkylaluminoxane is 1: 10-100: 0.1-2, preferred 1: 45: 1; Stirred 1-10 hour in 25-80 ℃ again; Preferably stirred 4 hours down, after finishing, use hexane wash again 3 times at 50 ℃; Afterwards solid is dried up with nitrogen, obtain the bar-shaped macropore mesoporous silicon oxide of load MAO;
The 8th step under nitrogen protection, joined the bar-shaped macropore mesoporous silicon oxide of load MAO in the reactor drum, added stirring solvent and processed slurries; In the container of crossing with nitrogen replacement in advance, solution is processed in the metallocene compound dissolving; Under 25-80 ℃ of agitation condition; Preferably under 30 ℃ of stirrings; Slowly the metallocene compound drips of solution is added in the reactor drum, counts bar-shaped macropore mesoporous silicon oxide (in silicon-dioxide): toluene in molar ratio: the amount ratio of two (n-butyl cyclopentadienyl) zirconium dichloride BUCP of metallocene compound is 1: 20-150: 2 * 10
-3-19 * 10
-3, stirring reaction 0.3-2 hour, the preferable amount ratio was 1: 45: 12.4 * 10
-3, to stir 0.5 hour, reaction is left standstill after finishing, and leaches liquid, with toluene and hexane wash, dries up with nitrogen, obtains said carried metallocene catalyst.
According to olefine polymerizing process of the present invention, said one or more alkene can carry out in the presence of solvent with contacting of said carried metallocene catalyst, and said solvent is preferably and replaces or unsubstituted alkane or replacement or unsubstituted aromatic hydrocarbons.When said alkane and aromatic hydrocarbons had substituting group, said substituting group was preferably halogenic substituent.More preferably, said solvent is one or more in hexane, pentane, heptane, benzene, toluene, methylene dichloride, chloroform and the methylene dichloride.
The consumption of said solvent can carry out appropriate selection according to concrete use occasion.Preferably, the consumption of said solvent makes that the concentration of said carried metallocene catalyst is 1 * 10
-8-1 * 10
-3Mol is preferably 1 * 10
-8-1 * 10
-5Mol.
According to olefine polymerizing process of the present invention, said one or more alkene carry out in the presence of the solution that contains aluminum alkyls and/or alkylaluminoxane with contacting preferably of said carried metallocene catalyst.That is,, preferably when carrying out polymerization, in reaction system, replenish and add the solution that contains aluminum alkyls and/or alkylaluminoxane according to olefine polymerizing process of the present invention.Be in the effect that aluminum alkyls and/or the alkylaluminoxane of alkylaluminoxane on loading on said carrier in the solution play the cleaning reaction poisonous substance, thereby make the metallocene compound that loads on the said carrier can bring into play katalysis better.
According to olefine polymerizing process of the present invention; When said one or more alkene carried out in the presence of the solution that is containing aluminum alkyls and/or alkylaluminoxane with contacting of said carried metallocene catalyst, whole aluminium and the mol ratio of the M in the said metallocene compound can be 100-3000 in said aluminum alkyls and the said alkylaluminoxane (comprise the alkylaluminoxane that loads on the said carrier and be in the alkylaluminoxane in the solution): 1.
Said aluminum alkyls can be the known various aluminum alkylss that are used as the promotor of metallocene catalyst of the technician of field of olefin polymerisation.Preferably, the alkyl in the said aluminum alkyls can be C
1-C
5Alkyl.More preferably, said aluminum alkyls is a triethyl aluminum.
The alkylaluminoxane that is in the solution can be identical with the kind that loads on alkylaluminoxane on the said carrier (that is, replenishing the alkylaluminoxane that the alkylaluminoxane that adds and said carried metallocene catalyst contain), also can difference; Be preferably identical.
According to olefine polymerizing process of the present invention, said alkene can be in ethene, terminal olefin and the diolefin one or more.Preferably, said alkene is ethene, C
3-C
101-alkene, C
4-C
8Diolefin in one or more.More preferably, said alkene is one or more in ethene, 1-butylene, 1-amylene and the 1-hexene.
According to olefine polymerizing process of the present invention, because the present invention is through using said carried metallocene catalyst to improve the efficient of polyreaction, so the present invention does not limit for said olefinic polymerization condition is special.Can be the known polymerizing condition of the technician of field of olefin polymerisation.Preferably, in metallocene compound, the concentration of said carried metallocene catalyst can be 1 * 10
-8-1 * 10
-5Mol.The polymeric temperature can be-78 ℃ to 100 ℃, is preferably 0 ℃-90 ℃; Pressure can be 0.01-10MPa, is preferably 0.01-2MPa.
Below in conjunction with embodiment the present invention is carried out detailed description.
In following examples, X-ray diffraction analysis is to carry out on the X-ray diffractometer of D8 Advance in the model available from company of German Bruker AXS company; TEM analysis is to carry out on the transmission electron microscope of Tecnai 20 in the model available from company of Dutch FEI Co.; Scanning electron microscope analysis is to carry out on the sem of XL-30 in the model available from U.S. FEI Co..Ultimate analysis is carried out on the instrument available from the model 7500CX of U.S. An Jielun company.Nitrogen adsorption-desorption experiment condition comprises: the U.S. Autosorb-1 of Kang Ta company nitrogen adsorption desorption appearance, sample was 200 ℃ of degassings 4 hours.
Preparation example 1
This preparation example is used for preparing the carried metallocene catalyst that olefine polymerizing process according to the present invention uses.
The 1st step joined 4.0 gram P123 (registration number at U.S. chemical abstract is the material of 9003-11-6, its average molecular mass Mn=5800) in the solution of hydrochloric acid and 128ml water of 16.4ml 37%, was stirred to P123 at 40 ℃ and dissolved fully;
In the 2nd step, 8.86 gram tetraethoxys are joined in the above-mentioned solution stirred 24 hours again at 40 ℃;
In the 3rd step, gained solution is transferred in the teflon-lined reaction kettle, 150 ℃ of crystallization 24 hours;
The 4th step is through obtaining former powder mesoporous material after filtration, washing, the drying;
The 5th step, former powder mesoporous material was under refluxad washed 24 hours with ethanol, removed template method obtains bar-shaped macroporous/mesoporous material (called after KKSBA-15).
With bar-shaped macroporous/mesoporous material KKSBA-15 400 ℃ of calcinings 10 hours under nitrogen protection, removing hydroxyl and remaining moisture, thereby obtain bar-shaped macroporous/mesoporous material through thermal activation.
0.25 gram is transferred in 250 milliliters of glass reactors after nitrogen is fully replaced through the bar-shaped macroporous/mesoporous material of thermal activation, adds 20 milliliters of purified toluene, 0.25 gram MAO (available from U.S. Albemarle Corporation) in 50 ℃ of stirrings 4 hours.After finishing, use 20 milliliters of hexane wash three times again, at last solid is dried up with nitrogen, obtaining load has the bar-shaped macroporous/mesoporous material of MAO (called after MAO/KKSBA-15).
Under nitrogen protection; The MAO/KKSBA-15 that obtains is all joined in 250 milliliters of glass reactors; Add 20 milliliters of purified toluene, under 30 ℃, two (n-butyl cyclopentadienyl) zirconium dichlorides that slowly drip 20.9 milligrams are (available from AlfaAesar; Article No. H27576), stirring reaction is 0.5 hour.After reaction finishes, leave standstill, leach liquid after the layering,, follow,, solid is dried up with nitrogen, obtain according to carried metallocene catalyst of the present invention (called after KKSBA-15-BU) with 40 milliliters of hexane wash twice with 10 milliliters of toluene wash three times.Come this carried metallocene catalyst is characterized with x-ray diffractometer (XRD), nitrogen adsorption-desorption experiment, ESEM, X-ray energy spectrometer and ICP ultimate analysis.
Fig. 1 is the little angle x-ray diffraction pattern of bar-shaped macropore mesoporous silicon oxide KKSBA-15, and Fig. 2 is the little angle x-ray diffraction pattern of carried metallocene catalyst KKSBA-15-BU.Can obviously find out by XRD spectra; Maller angle spectrum peak all appears in bar-shaped macropore mesoporous silicon oxide KKSBA-15 and carried metallocene catalyst KKSBA-15-BU, explains that the macropore KKSBA-15-BU of load metallocene has the peculiar two-dimentional hexagonal hole of mesoporous material road structure.
Fig. 3 and Fig. 4 are respectively the N of macropore meso-porous titanium dioxide silicon carrier KKSBA-15 and carried metallocene catalyst KKSBA-15-BU
2The adsorption desorption graphic representation, wherein, X-coordinate is a relative pressure, unit is p/p
0Fig. 4 shows that KKSBA-15-BU has the IV type thermo-isopleth of sharp-pointed capillary condensation speed, and this thermo-isopleth has the H1 hysteresis loop, and this shows that KKSBA-15-BU has the aperture size distribution of homogeneous.
Fig. 5 and Fig. 6 are respectively the graph of pore diameter distribution of macropore meso-porous titanium dioxide silicon carrier KKSBA-15 and carried metallocene catalyst KKSBA-15-BU, and wherein, X-coordinate is the aperture, and unit is nm.Can find out that by figure KKSBA-15 and KKSBA-15-BU have six sides' meso-hole structure, and the duct is very even.
Fig. 7 is a stereoscan photograph, and a is the stereoscan photograph of composite mesopore silica supports KKSBA-15, and b is the stereoscan photograph of carried metallocene catalyst KKSBA-15-BU.Can find out that by figure the microscopic appearance of KKSBA-15 and KKSBA-15-BU is bar-shaped, KKSBA-15-BU has mechanical property preferably in loading process.
Table 1 is the pore structure parameter of bar-shaped macropore mesoporous silicon oxide KKSBA-15 and carried metallocene catalyst KKSBA-15-BU.
Table 1 pore structure parameter
Data by last table 1 can find out, bar-shaped macropore mesoporous silicon oxide KKSBA-15 behind load metallocene, pore volume, specific surface area and aperture all reduce to some extent, this explanation metallocene in the load-reaction process enters into the inside of bar-shaped macropore mesoporous silicon oxide.
Ultimate analysis ICP result shows; Load the aluminium content of bar-shaped macropore mesoporous silicon oxide KKSBA-15-BU of two (n-butyl cyclopentadienyl) zirconium dichlorides (BUCP) of MAO (MAO) and metallocene compound be 14.6 weight %; The content of Zr is 0.5 weight %, and the mol ratio of Al/Zr is 100: 1.Learn through converting, be benchmark with the total amount of catalyzer, and the total content of MAO (MAO) and metallocene compound is 33.6 weight %, and the content of carrier is 66.4 weight %.
Present embodiment is used for explanation according to olefine polymerizing process of the present invention.
In 2 liters stainless steel polymermaking autoclave, respectively replace three times with nitrogen and ethene, add 200 milliliters of hexanes then; With still temperature rise to 80 ℃, add 800 milliliters of hexanes again, along with the adding of hexane; The concentration that adds 2 milliliters is triethyl aluminum (TEA) hexane solution of 1 mol; Then add 47.7 milligrams of KKSBA-15-BU, feed ethene pressure is risen to 1.0MPa and is maintained 1.0MPa, 70 ℃ of reactions 1 hour.Obtain 90 gram polyethylene particle powders, the bulk density of this polyethylene particle powder (BD) is 0.222g/ml, melting index MI
2.16=0.025g/10min.Confirm that through calculating the efficient of catalyzer is 1887gPE/gcath (that is, 3.4 * 10
7GPE/mol Zrh).
Present embodiment is used for explanation according to olefine polymerizing process of the present invention.
In 2 liters stainless steel polymermaking autoclave, respectively replace three times with nitrogen and ethene, add 200 milliliters of hexanes then; With still temperature rise to 70 ℃, add 800 milliliters of hexanes again, along with the adding of hexane; The concentration that adds 2 milliliters is triethyl aluminum (TEA) hexane solution and 10 milliliters of hexenes of 1 mol; The KKSBA-15-BU that then adds 44.6 milligrams fed ethene pressure is risen to 1.0MPa and is maintained 1.0MPa, 70 ℃ of reactions 1 hour.Obtain 68 gram polymkeric substance, the bulk density of this polymkeric substance (BD) is 0.205g/ml, melting index MI
2.16=0.058g/10min.Confirm that through calculating the efficient of catalyzer is 1525gPE/gcath (that is, 2.8 * 10
7GPE/mol Zrh).
Preparation Comparative Examples 1
This preparation Comparative Examples is used to explain that carrier is the preparation of the carried metallocene catalyst of ES955 silica gel.
With the 400 ℃ of calcinings 10 hours under nitrogen protection of ES955 silica gel, removing hydroxyl and remaining moisture, thereby obtain silica gel through the ES955 of thermal activation.
Under nitrogen protection, 0.9 gram ES955 silica gel is joined in 250 milliliters of glass reactors, add 1.0 gram MAO and 10mL toluene again; Under 50 ℃ of conditions; Behind the stirring reaction 4 hours,, use 20 milliliters of hexane wash three times again with toluene wash 3 times; At last solid is dried up with nitrogen, obtaining load has the ES955 of MAO (called after MAO/ES955).
Under nitrogen protection; MAO/ES955 is joined in 250 milliliters of glass reactors, add 20 milliliters of purified toluene (refluxing 24 hours), under 30 ℃ with sodium; Slowly drip two (normal-butyl-cyclopentadienyl moiety) zirconium dichlorides of metallocene compound of 44 milligrams, stirring reaction 0.5 hour.After reaction finishes, leave standstill, leach liquid,, follow,, solid is dried up with nitrogen, obtain carried metallocene catalyst (called after MAO/ES955-BU) with 40 milliliters of hexane wash twice with 10 milliliters of toluene wash three times.
Results of elemental analyses shows that the content of the aluminium among the ES955-BU is 32.4 weight %, and the content of Zr is 0.41 weight %, and the mol ratio of Al/Zr is 270: 1.
Preparation Comparative Examples 2
This preparation Comparative Examples is used to explain that metallocene compound is bicyclic pentadiene zirconium dichloride CpZrCl
2The preparation of carried metallocene catalyst.
Adopt and prepare routine 1 identical method and prepare carried metallocene catalyst, different is employing bicyclic pentadiene zirconium dichloride CpZrCl
2As metallocene compound, obtain carried metallocene catalyst (called after KKSBA-15-Cp).Results of elemental analyses shows that the aluminium content among the KKSBA-15-Cp is 24 weight %, and the content of Zr is 1 weight %, and the mol ratio of Al/Zr is 81: 1.
Comparative Examples 1
Adopt and carry out the homopolymerization of ethene with embodiment 1 identical method; Different is; The catalyzer that adopts adds 50 milligrams of ES955-BU for the ES955-BU of preparation Comparative Examples 1 preparation, and the result obtains 65g polyethylene particle powder; The bulk density of this polyethylene particle powder (BD) is 0.331g/ml, melting index: MI
2.16=0.119g/10min.Confirm that through calculating the efficient of catalyzer is 1300gPE/gcath (that is, 2.9 * 10
7GPE/mol Zrh).
Comparative Examples 2
Adopt and ethene and hexene are carried out copolymerization with embodiment 2 identical methods; Different is; The catalyzer that adopts adds 60 milligrams of ES955-BU for the ES955-BU of preparation Comparative Examples 1 preparation, obtains 60 gram polymkeric substance; The density of this polymer stacks (BD) is 0.299g/ml, and melting index is MI2.16=0.679g/10min.Confirm that through calculating the efficient of catalyzer is 1000gPE/gcath (that is, 2.2 * 10
7GPE/mol Zrh).
Comparative Examples 3
Adopt and carry out the homopolymerization of ethene with embodiment 1 identical method, different is that the catalyzer of employing is the KKSBA-15-Cp of preparation Comparative Examples 2 preparations.The result obtains 36g polyethylene particle powder, adds 93 milligrams of KKSBA-15-Cp, and the bulk density of this polyethylene particle powder (BD) is 0.30g/ml, melting index: MI
2.16=0.011g/10min.Confirm that through calculating the efficient of catalyzer is 387gPE/gcath (that is, 3.5 * 10
6GPE/mol Zrh).
Comparative Examples 4
Adopt and ethene and hexene are carried out copolymerization with embodiment 2 identical methods; Different is; The catalyzer that adopts adds 98 milligrams of KKSBA-15-Cp for the KKSBA-15-Cp of preparation Comparative Examples 2 preparations, obtains the multipolymer of 43 gram ethene and hexene; The density (BD) of the multipolymer heap of this ethene and hexene is 0.304g/ml, and melting index is MI
2.16=0.077g/10min.Confirm that through calculating the efficient of catalyzer is 439gPE/gcath (that is, 4.0 * 10
6GPE/mol Zrh).
Claims (13)
1. olefine polymerizing process, this method is included under the olefinic polymerization condition, and one or more alkene are contacted with carried metallocene catalyst; It is characterized in that; Said carried metallocene catalyst comprises carrier and loads on metallocene compound and the alkylaluminoxane on the said carrier, and said carrier is bar-shaped macropore mesoporous silicon oxide, and the most probable aperture of said bar-shaped macropore mesoporous silicon oxide is the 11-20 nanometer; Said metallocene compound has the structure shown in the formula 1
Formula 1
Wherein, R
1, R
2, R
3, R
4, R
5, R
1', R
2', R
3', R
4' and R
5' be hydrogen or C independently of one another
1-C
5Alkyl, and R
1, R
2, R
3, R
4And R
5In at least one be C
1-C
5Alkyl, R
1', R
2', R
3', R
4' and R
5' at least one be C
1-C
5Alkyl, M is a kind of in titanium, zirconium and the hafnium, X is a halogen.
2. olefine polymerizing process according to claim 1 wherein, is a benchmark with the total amount of said carried metallocene catalyst, and the total amount of said metallocene compound and alkylaluminoxane is 20-50 weight %, and the content of said carrier is 50-80 weight %.
3. olefine polymerizing process according to claim 1 and 2, wherein, the mol ratio of the M in aluminium in the said alkylaluminoxane and the said metallocene compound is 50-200: 1.
4. olefine polymerizing process according to claim 1, wherein, M is a zirconium, X is a chlorine.
5. olefine polymerizing process according to claim 1, wherein, the R in the said metallocene compound
1, R
1' be C
1-C
5Alkyl, and R
2, R
3, R
4, R
5, R
2', R
3', R
4' and R
5' being hydrogen, preferred said metallocene compound is two (n-butyl cyclopentadienyl) zirconium dichlorides; Alkyl in the said alkylaluminoxane is C
1-C
5Alkyl, preferred said alkylaluminoxane is a MAO.
6. olefine polymerizing process according to claim 1 and 2, wherein, the length of said carrier is the 2-20 micron, and length-to-diameter ratio is 2-8, and specific surface area is the 300-600 meters squared per gram, and pore volume is 0.3-1.5 milliliter/gram.
7. olefine polymerizing process according to claim 1, wherein, said carrier is made by the method that may further comprise the steps:
(1) template, water and HCl are stirred to dissolving under 25-60 ℃ of temperature;
(2) under 25-60 ℃ of temperature, stir more than 0.2 hour step (1) gained solution and tetraethoxy;
(3) with step (2) products therefrom crystallization under crystallization condition;
(4) be that the alcoholic solvent of 1-4 contacts with step (3) gained crystallization product and carbonatoms, with removed template method;
Said template is polyoxyethylene-polyoxytrimethylene-polyoxyethylene triblock copolymer.
8. olefine polymerizing process according to claim 7, wherein, said crystallization condition comprises: crystallization temperature is 90-180 ℃, crystallization time is 10-40 hour.
9. olefine polymerizing process according to claim 7; Wherein, Said crystallization product and carbonatoms are that the condition that the alcoholic solvent of 1-4 contacts comprises that temperature is 90-120 ℃, and the time is 10-40 hour, and crystallization product and carbonatoms are that the weight ratio of the alcoholic solvent of 1-4 is 1: 100-300.
10. according to claim 7 or 9 described olefine polymerizing process, wherein, said carbonatoms is that the alcoholic solvent of 1-4 is an ethanol.
11. olefine polymerizing process according to claim 7 wherein, is counted polyoxyethylene-polyoxytrimethylene-polyoxyethylene: water: hydrogenchloride=1: 9000-15000: 100-500 in molar ratio.
12. olefine polymerizing process according to claim 1, wherein, said alkene is one or more in ethene, terminal olefin and the diolefin, and preferred said alkene is ethene, C
3-C
101-alkene, C
4-C
8Diolefin in one or more.
13. method according to claim 1, wherein, said contact is carried out in solvent, and said olefinic polymerization condition comprises: in metallocene compound, the concentration of said carried metallocene catalyst is 1 * 10
-8-1 * 10
-5Mol, temperature are-78 ℃ to 100 ℃, and pressure is 0.01-10MPa.
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| CN103910930A (en) * | 2012-12-31 | 2014-07-09 | 中国科学院化学研究所 | Polypropylene intra-autoclave alloy having carbon nanotubes, preparation method for the alloy, and applications thereof |
| CN105017460A (en) * | 2015-06-25 | 2015-11-04 | 合肥蓝科新材料有限公司 | Nanometer gamma-LiAlO2-multiwalled carbon nanotube-reinforced polypropylene resin and preparation method thereof |
| CN105037598A (en) * | 2015-06-25 | 2015-11-11 | 合肥蓝科新材料有限公司 | Multi-walled carbon nano-tube reinforced polypropylene resin for automobile parts, and preparation method for multi-walled carbon nano-tube reinforced polypropylene resin |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103910930A (en) * | 2012-12-31 | 2014-07-09 | 中国科学院化学研究所 | Polypropylene intra-autoclave alloy having carbon nanotubes, preparation method for the alloy, and applications thereof |
| CN105017460A (en) * | 2015-06-25 | 2015-11-04 | 合肥蓝科新材料有限公司 | Nanometer gamma-LiAlO2-multiwalled carbon nanotube-reinforced polypropylene resin and preparation method thereof |
| CN105037598A (en) * | 2015-06-25 | 2015-11-11 | 合肥蓝科新材料有限公司 | Multi-walled carbon nano-tube reinforced polypropylene resin for automobile parts, and preparation method for multi-walled carbon nano-tube reinforced polypropylene resin |
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