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CN104558290B - One kind being used for catalyst component for olefin polymerization and catalyst - Google Patents

One kind being used for catalyst component for olefin polymerization and catalyst Download PDF

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CN104558290B
CN104558290B CN201310517877.3A CN201310517877A CN104558290B CN 104558290 B CN104558290 B CN 104558290B CN 201310517877 A CN201310517877 A CN 201310517877A CN 104558290 B CN104558290 B CN 104558290B
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malonic acid
ester
acid
allyl
malonate
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CN104558290A (en
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蔡晓霞
高明智
刘海涛
马晶
陈建华
马吉星
王军
胡建军
李昌秀
李现忠
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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Abstract

A kind of catalytic component for olefinic polymerization, it includes magnesium, titanium, halogen and Lewis alkali cpds, the Lewis alkali cpds include general formula(Ⅰ)Compound represented and compound selected from ether compound, benzoate compounds and phthalate compound;

Description

One kind being used for catalyst component for olefin polymerization and catalyst
Technical field
It is specific a kind of for the catalytic component of olefinic polymerization and comprising described the present invention relates to a kind of field of olefin polymerisation The catalyst of catalytic component.
Background technology
Ziegler-Natter catalyst is usually made of magnesium, titanium, halogen and Lewis alkali etc., and wherein Lewis alkali is to contain Some organic compounds of oxygen, nitrogen, phosphorus, silicon etc..The Nomenclature Composition and Structure of Complexes of Lewis alkali is bigger on the influence of the performance of catalyst, together A kind of feed postition that Lewis alkali is different is also obvious on the influence of the performance of catalyst.Currently, have document disclose it is special Structure malonic acid ester type compound is as Lewis alkali, but the activity of catalyst and isotacticity be not high, poor practicability.In addition, Special 1, the 3- bis- of ether group containing there are two is used in the catalytic component of olefinic polyreaction, there is document to disclose Ether compound is as Lewis alkali, such as 9,9- bis-(Methoxy)Fluorenes etc. has higher poly- when for propylene polymerization Activity and stereoselectivity are closed, but molecular weight distribution is narrow, poor processability, limits its application.
Invention content
For deficiency in the prior art, the catalytic component that the present invention provides a kind of for olefinic polymerization, preparation side Method and catalyst, the catalyst that the component obtains are used for olefinic polymerization, and there is higher catalytic activity, the polymer to have Higher isotacticity, melt index and wider molecular weight distribution.
According to an aspect of the invention, there is provided a kind of catalytic component for olefinic polymerization, it includes magnesium, titanium, Halogen and Lewis alkali cpds, the Lewis alkali cpds include general formula(Ⅰ)Compound represented and selected from ether compound, The compound of benzoate compounds and phthalate compound;
Wherein, R1And R2It is identical or different, it is selected from C1-C20Substituted or unsubstituted straight chained alkyl, branched alkyl, cycloalkanes Base, aryl, alkaryl, aralkyl, alkylene and fused ring aryl;R3And R4It is identical or different, it is selected from hydrogen and C1-C20Substitution or Unsubstituted straight chained alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl, alkylene and fused ring aryl, R3And R4It can It is optionally bonded cyclic or not cyclic.
Catalytic component according to the present invention, the Lewis alkali cpds include general formula(Ⅰ)Compound represented and General formula(Ⅱ)Shown in diether compound,
Wherein, RI、RII、RIII、RIV、RVAnd RVIIt is identical or different, it is hydrogen or C1-C18Hydrocarbyl group, and RVIIAnd RVIII It is identical or different, it is C1-C18Hydrocarbyl group;RI~RVIIIThe optionally bonded cyclization of one or more of group or not at Ring.
According to the present invention, the substituted straight chained alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl or alkene Alkyl, as straight chained alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl or alkylene carbon or hydrogen atom optionally Replaced by one or several hetero atoms, the hetero atom is selected from nitrogen, oxygen, sulphur, silicon, phosphorus or halogen atom.In the present invention, R3And R4 When bonded cyclization, double bond or hetero atom can also be contained in ring.
In the catalytic component of the present invention, it is preferable that the R1And R2Selected from C1-C10Substituted or unsubstituted straight chain Alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl and alkylene.
In the catalytic component of the present invention, the general formula(Ⅰ)Compound represented and general formula(Ⅱ)Compound represented Molar ratio be 1:50-50:1, preferably 1:20-20:1, more preferably 1:10-10:1, it is even more preferably 1:5-5:1.
In the catalytic component of the present invention, the general formula(Ⅰ)Compound represented can be selected from but be not limited only to:Two isobutyls Propylmalonic acid diethylester, di-n-butyl diethyl malonate, di-t-butyl diethyl malonate;Diisobutyl malonic acid dipropyl Ester, di-n-butyl dipropyl malonate, di-t-butyl dipropyl malonate, diisobutyl dibutyl malonate, di-n-butyl third Adipate, di-t-butyl dibutyl malonate, diisobutyl malonic acid diamyl ester, di-n-butyl malonic acid diamyl ester, two Tertiary butyl malonic acid diamyl ester, diisobutyl malonic acid dihexyl, di-n-butyl malonic acid dihexyl, di-t-butyl malonic acid two Own ester, two heptyl ester of diisobutyl malonic acid, two heptyl ester of di-n-butyl malonic acid, two heptyl ester of di-t-butyl malonic acid, dipropyl third Dipropyl malona-te, diisoamyl dipropyl malonate, two n-amyl malonic acid dipropyls, dihexyl dipropyl malonate, two are just Amyl malonic acid dipropyl, phenylethyl dipropyl malonate, phenyl methyl dipropyl malonate, phenyl propyl malonic acid dipropyl Ester, phenyl n-butylmalonic acid dipropyl, phenyl isobutyl propylmalonic acid dipropyl, phenyl isoamyl-malonic acid dipropyl, phenyl N-amyl malonic acid dipropyl, diphenylprop dipropyl malona-te, benzyl ethyl malonic acid dipropyl, benzyl methyl malonic acid dipropyl Ester, benzyl propylmalonic acid dipropyl, benzyl n-butylmalonic acid dipropyl, benzyl isobutyl group dipropyl malonate, benzyl are different Amyl malonic acid dipropyl, benzyl n-amyl malonic acid dipropyl, dibenzyl dipropyl malonate, two fourth of phenylethyl malonic acid Ester, phenyl methyl dibutyl malonate, phenyl propyl dibutyl malonate, phenyl n-butylmalonic acid dibutyl ester, phenyl isobutyl Propylmalonic acid dibutyl ester, phenyl isoamyl-malonic acid dibutyl ester, phenyl n-amyl malonic acid dibutyl ester, two fourth of diphenylprop diacid Ester, benzyl ethyl malonic acid dibutyl ester, benzyl methyl dibutyl malonate, benzyl propylmalonic acid dibutyl ester, benzyl normal-butyl Dibutyl malonate, benzyl isobutyl group dibutyl malonate, benzyl isoamyl-malonic acid dibutyl ester, benzyl n-amyl malonic acid two Butyl ester, dibenzyl dibutyl malonate, phenylethyl malonic acid diamyl ester, phenyl methyl malonic acid diamyl ester, phenyl propyl third Diacid diamyl ester, phenyl n-butylmalonic acid diamyl ester, phenyl isobutyl propylmalonic acid diamyl ester, phenyl isoamyl-malonic acid diamyl Ester, phenyl n-amyl malonic acid diamyl ester, diphenylprop diacid diamyl ester, benzyl ethyl malonic acid diamyl ester, benzyl methyl third Diacid diamyl ester, benzyl propylmalonic acid diamyl ester, benzyl n-butylmalonic acid diamyl ester, benzyl isobutyl propylmalonic acid diamyl Ester, benzyl isoamyl-malonic acid diamyl ester, benzyl n-amyl malonic acid diamyl ester, dibenzyl propylmalonic acid diamyl ester, phenylethyl Malonic acid dicyclohexyl maleate, phenyl methyl malonic acid dicyclohexyl maleate, phenyl propyl malonic acid dicyclohexyl maleate, phenyl n-butylmalonic acid Dicyclohexyl maleate, phenyl isobutyl propylmalonic acid dicyclohexyl maleate, phenyl isoamyl-malonic acid dicyclohexyl maleate, phenyl n-amyl malonic acid two Cyclohexyl, diphenylprop dicyclohexyl sulfosuccinnate ester, benzyl ethyl malonic acid dicyclohexyl maleate, benzyl methyl malonic acid dicyclohexyl maleate, benzyl Base propylmalonic acid dicyclohexyl maleate, benzyl n-butylmalonic acid dicyclohexyl maleate, benzyl isobutyl propylmalonic acid dicyclohexyl maleate, benzyl are different Amyl malonic acid dicyclohexyl maleate, benzyl n-amyl malonic acid dicyclohexyl maleate, dibenzyl propylmalonic acid dicyclohexyl maleate, phenyl methyl the third two Diphenyl phthalate, phenyl propyl diphenyl malonate, phenyl n-butylmalonic acid diphenyl ester, phenyl isobutyl propylmalonic acid diphenyl ester, Phenyl isoamyl-malonic acid diphenyl ester, phenyl n-amyl malonic acid diphenyl ester, diphenyl diphenyl malonate, benzyl ethyl the third two Diphenyl phthalate, benzyl methyl diphenyl malonate, benzyl propylmalonic acid diphenyl ester, benzyl n-butylmalonic acid diphenyl ester, benzyl Base isobutyl group diphenyl malonate, benzyl isoamyl-malonic acid diphenyl ester, benzyl n-amyl malonic acid diphenyl ester, dibenzyl the third two Diphenyl phthalate, fluorenyl methyl malonic acid dicyclohexyl maleate, fluorenyl propylmalonic acid dicyclohexyl maleate, two hexamethylene of fluorenyl n-butylmalonic acid Ester, fluorenyl isobutyl propylmalonic acid dicyclohexyl maleate, fluorenyl isoamyl-malonic acid dicyclohexyl maleate, two hexamethylene of fluorenyl n-amyl malonic acid Ester, two fluorenyl malonic acid dicyclohexyl maleates, allyl methyl diphenyl malonate, allyl propylmalonic acid diphenyl ester, allyl N-butylmalonic acid diphenyl ester, allyl isobutyl group diphenyl malonate, allyl isoamyl-malonic acid diphenyl ester, allyl are just Amyl malonic acid diphenyl ester, diallyl diphenyl malonate, allyl methyl dimethyl malenate, allyl propylmalonic acid Dimethyl ester, allyl n-butylmalonic acid dimethyl ester, allyl isobutyl group dimethyl malenate, allyl isoamyl-malonic acid two Methyl esters, allyl n-amyl malonic acid dimethyl ester, diallyl dimethyl malenate, allyl methyl diethyl malonate, alkene Propyl propylmalonic acid diethylester, allyl diethyl butylmalonate, allyl iso-butyl diethyl malonate, allyl Isoamyl-malonic acid diethylester, allyl n-amyl malonic acid diethylester, diallyl diethyl malonate, allyl methyl third Dipropyl malona-te, allyl propylmalonic acid dipropyl, allyl n-butylmalonic acid dipropyl, allyl isobutyl propylmalonic acid Dipropyl, allyl isoamyl-malonic acid dipropyl, allyl n-amyl malonic acid dipropyl, diallyl malonic acid dipropyl Ester, allyl methyl dibutyl malonate, allyl propylmalonic acid dibutyl ester, allyl n-butylmalonic acid dibutyl ester, alkene Propyl isobutyl group dibutyl malonate, allyl isoamyl-malonic acid dibutyl ester, allyl n-amyl malonic acid dibutyl ester, diene Propylmalonic acid dibutyl ester, allyl methyl malonic acid diamyl ester, allyl propylmalonic acid diamyl ester, allyl normal-butyl third Diacid diamyl ester, allyl isobutyl propylmalonic acid diamyl ester, allyl isoamyl-malonic acid diamyl ester, allyl n-pentyl the third two Sour diamyl ester, diallyl malonic acid diamyl ester, allyl methyl malonic acid dicyclohexyl maleate, two hexamethylene of allyl propylmalonic acid Ester, allyl n-butylmalonic acid dicyclohexyl maleate, allyl isobutyl propylmalonic acid dicyclohexyl maleate, allyl isoamyl-malonic acid two Cyclohexyl, allyl n-amyl malonic acid dicyclohexyl maleate and diallyl malonic acid dicyclohexyl maleate, are preferably selected from diisobutyl third Diethyl adipate, di-n-butyl diethyl malonate, di-t-butyl diethyl malonate;Diisobutyl dipropyl malonate, two N-butylmalonic acid dipropyl, di-t-butyl dipropyl malonate, diethyl benzyl malonate, benzyl malonic acid dipropyl, benzene Base ethyl malonic acid diethylester, phenylethyl dipropyl malonate, dipropyl diethyl malonate, dipropyl propylmalonic acid dipropyl Ester, diallyl diethyl malonate and diallyl dipropyl malonate.
In the catalytic component of the present invention, the general formula(Ⅱ)Shown in diether compound be selected from 9,9- it is bis-(Methoxy Ylmethyl)Fluorenes, 2- isopropyl -2- isopentyl -1,3- dimethoxy propane, 2,2- diisobutyls -1,3- dimethoxy propane and 9,9- bis-(Methoxy)Fluorenes, 1,2- phenylenes dibenzoate and 2- isopropyl -2- cyclopenta -1,3- dimethoxy third Alkane.
In the catalytic component of the present invention, in the catalytic component, in the catalytic component, the content of magnesium is The content of 10-30wt%, titanium are 1-5wt%, general formula(Ⅰ)The content of compound represented is 1-20wt%, general formula(Ⅱ)Shown in two The content of ether compound is 1-20wt%.
According to another aspect of the present invention, a kind of method preparing above-mentioned catalytic component is provided, including following Step:
1)Magnesium compound is dissolved in containing general formula(Ⅰ)In the system of compound represented, precipitation agent is added, solid is precipitated Object;
2)With titanium compound processing step 1)The solids of precipitation, with titanium compound handle solids during and/ Or general formula is added before processing(Ⅱ)Compound represented.
Wherein step 1)In " magnesium compound is dissolved in containing general formula(Ⅰ)In the system of compound represented " comprising first by magnesium Compound is dissolved in dicyandiamide solution and obtains solution, adds general formula(Ⅰ)Compound represented;Also include by magnesium compound be dissolved in containing General formula(Ⅰ)In the system that compound represented and dicyandiamide solution collectively constitute.
In the above-mentioned methods, the precipitation agent such as can be selected from metal halide, such as halogenated titanium, iron halide, zinc halide.Its In, preferably halogenated titanium, such as titanium tetrachloride or titanium tetrabromide;More preferable titanium tetrachloride.
In the present invention, the magnesium compound is selected from magnesium dihalide, the hydrate of magnesium dihalide or alcohol adduct and dihalide The derivative that one of halogen atom is replaced by oxyl or halogenated oxyl in magnesium molecular formula;Preferably magnesium dihalide or two The alcohol adduct of magnesium halide, such as magnesium dichloride, dibrominated magnesium, magnesium diiodide and their alcohol adduct.
In the present invention, it is TiXm (OR that general formula, which can be selected, in the titanium compound1) 4-m compound, R in formula1For C1-C20 Alkyl, X is halogen, m=1~4.Such as:Titanium tetrachloride, titanium tetrabromide, titanium tetra iodide, four titanium butoxides, purity titanium tetraethoxide, One chlorine triethoxy titanium, dichlorodiethyl oxygroup titanium, one ethanolato-titanium of trichlorine, preferably titanium tetrachloride.
It may be selected to prepare the present invention's by following methods(Solid)Catalytic component, but catalysis according to the present invention The preparation method of agent is without being limited thereto.
First, magnesium compound is dissolved in and is made of organic epoxy compound object, organic phosphorus compound and inert diluent In dicyandiamide solution, after forming homogeneous solution, in special construction precipitation additive, i.e., above-mentioned general formula(Ⅰ)In the presence of compound, with titanizing Object mixing is closed, solids is precipitated in heating;This solids is handled using electron donor compound, makes its appendix in solids On, when necessary, then with titanium tetrahalide or titanium tetrahalide and inert diluent solids is handled.
Above-mentioned organic epoxy compound object, organic phosphorus compound etc. are disclosed in Chinese patent CN85100997, related Content is incorporated herein by reference.
It is emphasized that magnesium compound, may be dissolved in the dicyandiamide solution containing organic epoxide and organic phosphorus compound In.Wherein organic epoxy compound object include carbon atom number in 2~8 aliphatic olefin, alkadienes or halogenated aliphatic alkene or At least one of oxide, glycidol ether and inner ether of alkadienes.Particular compound is such as:Ethylene oxide, propylene oxide, ring Oxygen butane, butadiene oxide, butadiene double oxide, epoxychloropropane, methyl glycidyl ether, diglycidyl ether, four Hydrogen furans.
Wherein organic phosphorus compound includes the hydrocarbyl carbonate or halogenated hydrocarbons base ester of orthophosphoric acid or phosphorous acid, specifically such as:Orthophosphoric acid Trimethyl, orthophosphoric acid triethyl, orthophosphoric acid tributyl, orthophosphoric acid triphenylmethyl methacrylate, Trimethyl phosphite, triethyl phosphite, phosphorous Sour tributyl, phosphorous triphenyl phosphate methyl esters.
According to another method, magnesium compound is mixed with organic alcohol compound and atent solvent, rising temperature for dissolving is at uniform Solution, in above-mentioned general formula(Ⅰ)It in the presence of compound, mixes, heats up with titanium compound, solids is precipitated, this solids uses To general formula(Ⅱ)Shown in diether compound handled, make its appendix on solids, when necessary, then with titanium tetrahalide or Titanium tetrahalide and inert diluent handle solids.
Specifically list several methods for preparing catalyst below, rather than by the system of catalyst according to the present invention It is standby to be defined in this.
It prepares according to the method disclosed in patent CN85100997, first, magnesium compound is dissolved in by organic epoxidation In the dicyandiamide solution for closing object, organic phosphorus compound and inert diluent composition, mixed with titanium compound after forming homogeneous solution, Special construction precipitation additive, that is, above-mentioned general formula(Ⅰ)In the presence of compound, at -40~50 DEG C, preferably at -35~0 DEG C, titanizing is closed Object instills above-mentioned magnesium halide solution, then reaction mixture is warming up to 60~80 DEG C, and general formula is added(Ⅱ)Shown in two ethers Object is closed, suspension is stirred at this temperature 0~3 hour, mother liquor is filtered off, solids is obtained after inert diluent washs, then It is handled 1~5 time at a temperature of 60~130 DEG C with the halide of titanium and the mixture of inert diluent, is washed with inert diluent Solids obtains solid catalyst after dry.In terms of every mole of magnesium, the dosage of organic epoxy compound object is 0.2~10 mole;Have The dosage of machine phosphorus compound is 0.1~3 mole;Above-mentioned general formula(Ⅰ)0.001~30 mole of the dosage of compound, preferably 0.05~ 15 moles;3~40 moles of titanium compound, preferably 5~30 moles;General formula(Ⅱ)Shown in the dosage of diether compound be 0.005~15, preferably 0.05~5 mole.
According to another aspect of the present invention, a kind of catalyst for olefinic polyreaction is provided, it includes under State the reaction product of component:
A. above-mentioned catalytic component;
B. alkyl aluminum compound;
C. optionally, external electron donor component.
In above-mentioned catalyst system, the general formula of the alkyl aluminum compound is AlRnX3-n, R is hydrogen or C in formula1-C20Hydrocarbon Base, X are halogen, 0 n≤3 <.Specifically it can be selected from triethyl aluminum, tri-propyl aluminum, three n-butylaluminums, triisobutyl aluminium, three n-octyls Aluminium, triisobutyl aluminium, a hydrogen diethyl aluminum, a hydrogen diisobutyl aluminum, aluminium diethyl monochloride, a chloro-di-isobutyl aluminum, sesquialter second Base aluminium chloride, ethyl aluminum dichloride, preferably triethyl aluminum, triisobutyl aluminium.
" optionally, the external electron donor component " means as needed, and selection adds or be not added with external electron donor chemical combination Object.For need stereoregularity very high olefin polymer in application, 3 need to be added)External donor compound, such as general formula (R2)kSi(OR3)4-kShown in organo-silicon compound, 0≤k≤3, R in formula2Selected from halogen, hydrogen atom and C1-C20Alkyl, ring Alkyl, aryl, halogenated alkyl or amino, R3For C1-C20Alkyl, naphthenic base, aryl, halogenated alkyl or amino.Such as:Front three Methoxylsilane, trimethylethoxysilane, dimethyldimethoxysil,ne, dimethyl diethoxysilane, diphenyl two Methoxy silane, diphenyl diethoxy silane, phenyl triethoxysilane, phenyltrimethoxysila,e, vinyl trimethoxy Base silane, Cyclohexyl Methyl Dimethoxysilane, methyl-t-butyldimethoxysilane, preferably cyclohexyl methyl dimethoxy silicon Alkane, dimethoxydiphenylsilane.
In above-mentioned catalyst system, the component 1)With component 2)Molar ratio with titanium:Aluminium is calculated as 1:(5-1000), it is excellent Select 1:(25-100);The component 3)With component 1)Molar ratio with external electron donor:Titanium is calculated as 0-500:1, preferably 25-100: 1.When component 3)When external electron donor is above-mentioned organo-silicon compound, then the component 3)With component 1)Molar ratio with silicon: Titanium is calculated as 0-500:1, preferably 25-100:1
According to another aspect of the present invention, a kind of Prepolymerized catalyst system for olefinic polymerization, institute are provided It includes that a kind of above-mentioned catalytic component or above-mentioned catalyst system are carried out with alkene obtained by prepolymerization to state pre-polymerized catalyst Prepolymer, pre-polymerization multiple be 0.1~1000g olefin polymers/g ingredients of solid catalyst.
In the present invention, it is preferred to which pre-polymerization multiple is about 0.2~500g polymer/g ingredients of solid catalyst.Prepolymerization Process can in a liquid or in gas phase be carried out at a temperature of -20 to 80 DEG C, preferably 0~50 DEG C.Prepolymerized step can To be carried out as the part in continuous polymerization technique is online, or independently carried out in intermittently operated.
According to another aspect of the present invention, a kind of method for olefinic polymerization is provided, the alkene is above-mentioned to urge It is polymerize in the presence of agent component, above-mentioned catalyst system or the Prepolymerized catalyst system.
The catalyst of the present invention can be directly added into reactor in polymerization process or catalyst can be added Prepolymerization is carried out before first polymer reactor and obtains pre-polymerized catalyst, and alkene carries out in the presence of pre-polymerized catalyst Subsequent polymerisation.
In the present invention, the general formula of the preferably described alkene is CH2=CHR, R are hydrogen or C1-C12Alkyl or aryl group, more It is preferred that the alkene is ethylene or propylene.
The olefinic polyreaction of the present invention is carried out according to well known polymerization, can be carried out in liquid phase or gas phase, or Person can also carry out under the operation that liquid and gas polymerization stage combines.Using conventional technique such as slurry process, gas phase fluidization Bed etc., wherein alkene be selected from ethylene, propylene, 1- butylene, 4-methyl-1-pentene and 1- hexenes, the homopolymerization of special propylene with or The combined polymerization of other alkene of propylene.Preferably it is to use following reaction condition:0~150 DEG C of polymerization temperature, preferably 60~90 DEG C. Polymerization pressure is 0.01~10MPa.
According to the present invention, in the preparation process of catalytic component, general formula is added(Ⅰ)Compound represented and general formula(Ⅱ) Shown in diether compound, the good fluidity of the catalyst of gained, particle shape is good, even particle size distribution, the catalysis of gained The high comprehensive performance of agent.When the catalyst is used for olefinic polymerization, especially propylene polymerization, there is higher activity, obtain Polymer stereoregularity is high, molecular weight distribution that melt index is good and wider.
Specific implementation mode
Example given below is in order to further illustrate the present invention, rather than to carry out any limitation to the present invention.
Test method
Polymer isotactic index II:It is measured using heptane extraction process(Heptane boiling extracting 6 hours):2 grams of dry polymerizations Object sample is placed in extractor after being extracted 6 hours with boiling heptane, residue is dried to the polymer weight obtained by constant weight (g)Ratio with 2 is isotactic index.
Melt index MI:Using fusion index instrument under 230 DEG C, 2.16kg pressure, according to ASTM D1238-99《With squeeze Compactibility meter measures the standard test method of thermoplasticity fusing flow rate》It measures.
Polymer molecular weight and molecular weight distribution:It is oozed using Waters companies Waters Alliance GPC2000 gels Saturating chromatograph measures, and 1,2,4- trichloro-benzenes is solvent, and styrene is standard specimen.
Embodiment 1
In the reactor being sufficiently displaced from by high pure nitrogen, magnesium chloride 4.8g, toluene 95mL, epoxy chloropropionate are sequentially added Alkane 4mL, tributyl phosphate 12.5mL are warming up to 50 DEG C, and maintain 2.5h under stirring, solid is completely dissolved, and diisobutyl is added Diethyl malonate 10mmol, continues to 1h.Solution is cooled to -25 DEG C hereinafter, TiCl is added dropwise in 1h4Drop in 56mL, 1h Add TiCl456mL drips and is at the uniform velocity warming up to 80 DEG C, solids is gradually precipitated in temperature-rise period, is added to the solids 6mmol9,9- are bis-(Methoxy)Fluorenes maintains temperature 1h, after filtering, is washed twice, obtained solid with toluene 70mL respectively Sediment.Then toluene 60mL and TiCl are added into sediment440mL is warming up to 110 DEG C, maintains 2h, filtering;Same operation It is repeated once.And then three times, the time is respectively 10min to washing precipitate, adds hexane at 110 DEG C with toluene 70mL 60mL is washed twice, and obtains ingredient of solid catalyst.
Embodiment 2
Method is with embodiment 1, the difference is that substituting diisobutyl malonic acid using di-n-butyl diethyl malonate Diethylester.
Embodiment 3
Method is with embodiment 1, the difference is that substituting diisobutyl malonic acid two using dipropyl diethyl malonate Ethyl ester.
Embodiment 4
Method is with embodiment 1, the difference is that substituting diisobutyl malonic acid using diallyl diethyl malonate Diethylester.
Embodiment 5
Method is with embodiment 1, the difference is that being substituted using 2- isopropyl -2- isopentyl -1,3- dimethoxy propanes 9,9- is bis-(Methoxy)Fluorenes.
Embodiment 6
Method is with embodiment 1, the difference is that diisobutyl diethyl malonate addition 2mmol;9,9- is bis-(Methoxy Ylmethyl)Fluorenes addition 10mmol;
Embodiment 7
Method is with embodiment 1, the difference is that diisobutyl diethyl malonate addition 16mmol;9,9- is bis-(First Oxygroup methyl)Fluorenes addition 4mmol.
Comparative example 1
Method is with embodiment 1, the difference is that substituting diisobutyl diethyl malonate using phthalic anhydride.
Comparative example 2
Method is with embodiment 1, the difference is that it is bis- to substitute 9,9- using diisobutyl diethyl malonate(Methoxy methyl Base)Fluorenes.
Propylene polymerization
Volume is the stainless steel cauldron of 5L, and after gaseous propylene is sufficiently displaced from, AlEt32.5mmol, methyl cyclohexane is added Base dimethoxysilane(CHMMS)0.l mmol add above-described embodiment and the ingredient of solid catalyst 8-10mg of comparative example And 1.2L hydrogen, it is passed through liquid propene 2.3L, is warming up to 70 DEG C, maintains this temperature 1 hour.Cooling, pressure release obtain PP powder Material.Data are shown in Table 1.
Table 1
The data from table 1 are it is known that according to catalyst provided by the invention(Such as embodiment 1-7)With in the prior art (Comparative example 1 and 2)In catalytic component containing only general formula(Ⅰ)Compound represented or general formula(Ⅱ)Shown in diether compound It compares, shows certain synergistic effect, there is very excellent comprehensive performance, not only there is higher catalytic activity, and Resulting polymers have higher isotacticity, it is often more important that, resulting polymers have wider molecular weight distribution, are conducive to gather Close shaping for object.
It should be noted that embodiment described above is only used for explaining the present invention, do not constitute to any of the present invention Limitation.By referring to exemplary embodiments, invention has been described, it should be appreciated that word used in it is descriptive With explanatory vocabulary, rather than limited vocabulary.The present invention can be made within the scope of the claims by regulation Modification, and the present invention is revised in without departing substantially from scope and spirit of the present invention.Although the present invention described in it relates to And specific method, material and embodiment, it is not intended that the present invention is limited to particular case disclosed in it, on the contrary, this hair It is bright to can be extended to other all methods and applications with the same function.

Claims (20)

1. a kind of catalytic component for olefinic polymerization, it includes magnesium, titanium, halogen and Lewis alkali cpds, the Lewis Alkali cpd includes general formula (I) compound represented and the diether compound shown in the general formula (II);General formula (I) institute The molar ratio of the compound shown and general formula (II) compound represented is 1:5-4:1,
Wherein, R1And R2It is identical or different, it is selected from C1-C20Substituted or unsubstituted straight chained alkyl, branched alkyl, naphthenic base, virtue Base, alkaryl, aralkyl, alkylene and fused ring aryl;R3And R4It is identical or different, it is selected from hydrogen and C1-C20Substitution or unsubstituted Straight chained alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl, alkylene and fused ring aryl, R3And R4Optionally It is bonded cyclic or not cyclic;
Wherein, RI、RII、RIII、RIV、RVAnd RVIIt is identical or different, it is hydrogen or C1-C18Hydrocarbyl group, and RVIIAnd RVIIIIt is identical Or it is different, it is C1-C18Hydrocarbyl group;RI-RVIIIOne or more of group it is optionally bonded cyclic or not cyclic;
The catalytic component is prepared by method comprising the following steps:
1) magnesium compound is dissolved in the system containing general formula (I) compound represented, precipitation agent is added, solids is precipitated;
2) use titanium compound processing step 1) be precipitated solids, with titanium compound handle solids during and/or place Diether compound shown in general formula (II) is added before reason.
2. catalytic component according to claim 1, which is characterized in that the R1And R2Selected from C1-C10Substitution or do not take Straight chained alkyl, branched alkyl, naphthenic base, aryl, alkaryl, aralkyl and the alkylene in generation.
3. catalytic component according to claim 1, which is characterized in that general formula (I) compound represented and general formula (II) molar ratio of compound represented is 5:3-4:1.
4. catalytic component according to claim 1, which is characterized in that general formula (I) compound represented and general formula (II) molar ratio of compound represented is 1:5-5:3.
5. catalytic component according to claim 1, which is characterized in that general formula (I) compound represented is selected from two Iso-butyl diethyl malonate, di-n-butyl diethyl malonate, di-t-butyl diethyl malonate;Diisobutyl malonic acid two Propyl ester, di-n-butyl dipropyl malonate, di-t-butyl dipropyl malonate, diisobutyl dibutyl malonate, di-n-butyl Dibutyl malonate, di-t-butyl dibutyl malonate, diisobutyl malonic acid diamyl ester, di-n-butyl malonic acid diamyl ester, Di-t-butyl malonic acid diamyl ester, diisobutyl malonic acid dihexyl, di-n-butyl malonic acid dihexyl, di-t-butyl malonic acid Dihexyl, two heptyl ester of diisobutyl malonic acid, two heptyl ester of di-n-butyl malonic acid, two heptyl ester of di-t-butyl malonic acid, dipropyl Dipropyl malonate, diisoamyl dipropyl malonate, two n-amyl malonic acid dipropyls, dihexyl dipropyl malonate, two N-amyl malonic acid dipropyl, phenylethyl dipropyl malonate, phenyl methyl dipropyl malonate, phenyl propyl malonic acid two Propyl ester, phenyl n-butylmalonic acid dipropyl, phenyl isobutyl propylmalonic acid dipropyl, phenyl isoamyl-malonic acid dipropyl, benzene Base n-amyl malonic acid dipropyl, diphenylprop dipropyl malona-te, benzyl ethyl malonic acid dipropyl, benzyl methyl malonic acid two Propyl ester, benzyl propylmalonic acid dipropyl, benzyl n-butylmalonic acid dipropyl, benzyl isobutyl group dipropyl malonate, benzyl Isoamyl-malonic acid dipropyl, benzyl n-amyl malonic acid dipropyl, dibenzyl dipropyl malonate, phenylethyl malonic acid two Butyl ester, phenyl methyl dibutyl malonate, phenyl propyl dibutyl malonate, phenyl n-butylmalonic acid dibutyl ester, phenyl are different Butylmalonic acid dibutyl ester, phenyl isoamyl-malonic acid dibutyl ester, phenyl n-amyl malonic acid dibutyl ester, diphenylprop diacid two Butyl ester, benzyl ethyl malonic acid dibutyl ester, benzyl methyl dibutyl malonate, benzyl propylmalonic acid dibutyl ester, the positive fourth of benzyl Propylmalonic acid dibutyl ester, benzyl isobutyl group dibutyl malonate, benzyl isoamyl-malonic acid dibutyl ester, benzyl n-amyl malonic acid Dibutyl ester, dibenzyl dibutyl malonate, phenylethyl malonic acid diamyl ester, phenyl methyl malonic acid diamyl ester, phenyl propyl Malonic acid diamyl ester, phenyl n-butylmalonic acid diamyl ester, phenyl isobutyl propylmalonic acid diamyl ester, phenyl isoamyl-malonic acid two Pentyl ester, phenyl n-amyl malonic acid diamyl ester, diphenylprop diacid diamyl ester, benzyl ethyl malonic acid diamyl ester, benzyl methyl Malonic acid diamyl ester, benzyl propylmalonic acid diamyl ester, benzyl n-butylmalonic acid diamyl ester, benzyl isobutyl propylmalonic acid diamyl Ester, benzyl isoamyl-malonic acid diamyl ester, benzyl n-amyl malonic acid diamyl ester, dibenzyl propylmalonic acid diamyl ester, phenylethyl Malonic acid dicyclohexyl maleate, phenyl methyl malonic acid dicyclohexyl maleate, phenyl propyl malonic acid dicyclohexyl maleate, phenyl n-butylmalonic acid Dicyclohexyl maleate, phenyl isobutyl propylmalonic acid dicyclohexyl maleate, phenyl isoamyl-malonic acid dicyclohexyl maleate, phenyl n-amyl malonic acid two Cyclohexyl, diphenylprop dicyclohexyl sulfosuccinnate ester, benzyl ethyl malonic acid dicyclohexyl maleate, benzyl methyl malonic acid dicyclohexyl maleate, benzyl Base propylmalonic acid dicyclohexyl maleate, benzyl n-butylmalonic acid dicyclohexyl maleate, benzyl isobutyl propylmalonic acid dicyclohexyl maleate, benzyl are different Amyl malonic acid dicyclohexyl maleate, benzyl n-amyl malonic acid dicyclohexyl maleate, dibenzyl propylmalonic acid dicyclohexyl maleate, phenyl methyl the third two Diphenyl phthalate, phenyl propyl diphenyl malonate, phenyl n-butylmalonic acid diphenyl ester, phenyl isobutyl propylmalonic acid diphenyl ester, Phenyl isoamyl-malonic acid diphenyl ester, phenyl n-amyl malonic acid diphenyl ester, diphenyl diphenyl malonate, benzyl ethyl the third two Diphenyl phthalate, benzyl methyl diphenyl malonate, benzyl propylmalonic acid diphenyl ester, benzyl n-butylmalonic acid diphenyl ester, benzyl Base isobutyl group diphenyl malonate, benzyl isoamyl-malonic acid diphenyl ester, benzyl n-amyl malonic acid diphenyl ester, dibenzyl the third two Diphenyl phthalate, fluorenyl methyl malonic acid dicyclohexyl maleate, fluorenyl propylmalonic acid dicyclohexyl maleate, two hexamethylene of fluorenyl n-butylmalonic acid Ester, fluorenyl isobutyl propylmalonic acid dicyclohexyl maleate, fluorenyl isoamyl-malonic acid dicyclohexyl maleate, two hexamethylene of fluorenyl n-amyl malonic acid Ester, two fluorenyl malonic acid dicyclohexyl maleates, allyl methyl diphenyl malonate, allyl propylmalonic acid diphenyl ester, allyl N-butylmalonic acid diphenyl ester, allyl isobutyl group diphenyl malonate, allyl isoamyl-malonic acid diphenyl ester, allyl are just Amyl malonic acid diphenyl ester, diallyl diphenyl malonate, allyl methyl dimethyl malenate, allyl propylmalonic acid Dimethyl ester, allyl n-butylmalonic acid dimethyl ester, allyl isobutyl group dimethyl malenate, allyl isoamyl-malonic acid two Methyl esters, allyl n-amyl malonic acid dimethyl ester, diallyl dimethyl malenate, allyl methyl diethyl malonate, alkene Propyl propylmalonic acid diethylester, allyl diethyl butylmalonate, allyl iso-butyl diethyl malonate, allyl Isoamyl-malonic acid diethylester, allyl n-amyl malonic acid diethylester, diallyl diethyl malonate, allyl methyl third Dipropyl malona-te, allyl propylmalonic acid dipropyl, allyl n-butylmalonic acid dipropyl, allyl isobutyl propylmalonic acid Dipropyl, allyl isoamyl-malonic acid dipropyl, allyl n-amyl malonic acid dipropyl, diallyl malonic acid dipropyl Ester, allyl methyl dibutyl malonate, allyl propylmalonic acid dibutyl ester, allyl n-butylmalonic acid dibutyl ester, alkene Propyl isobutyl group dibutyl malonate, allyl isoamyl-malonic acid dibutyl ester, allyl n-amyl malonic acid dibutyl ester, diene Propylmalonic acid dibutyl ester, allyl methyl malonic acid diamyl ester, allyl propylmalonic acid diamyl ester, allyl normal-butyl third Diacid diamyl ester, allyl isobutyl propylmalonic acid diamyl ester, allyl isoamyl-malonic acid diamyl ester, allyl n-pentyl the third two Sour diamyl ester, diallyl malonic acid diamyl ester, allyl methyl malonic acid dicyclohexyl maleate, two hexamethylene of allyl propylmalonic acid Ester, allyl n-butylmalonic acid dicyclohexyl maleate, allyl isobutyl propylmalonic acid dicyclohexyl maleate, allyl isoamyl-malonic acid two Cyclohexyl, allyl n-amyl malonic acid dicyclohexyl maleate and diallyl malonic acid dicyclohexyl maleate.
6. catalytic component according to claim 1, which is characterized in that general formula (I) compound represented is selected from two Iso-butyl diethyl malonate, di-n-butyl diethyl malonate, di-t-butyl diethyl malonate, diisobutyl malonic acid two Propyl ester, di-n-butyl dipropyl malonate, di-t-butyl dipropyl malonate, diethyl benzyl malonate, benzyl malonic acid two Propyl ester, ethyl benzoic acid, phenylethyl dipropyl malonate, dipropyl diethyl malonate, dipropyl the third two Sour dipropyl, diallyl diethyl malonate and diallyl dipropyl malonate.
7. catalytic component according to claim 1, which is characterized in that diether compound shown in the general formula (II) Selected from bis- (methoxy) fluorenes of 9,9-, 2- isopropyl -2- isopentyl -1,3- dimethoxy propanes, 2,2- diisobutyls -1,3- Dimethoxy propane and (methoxy) fluorenes of 9,9- bis- and 2- isopropyl -2- cyclopenta -1,3- dimethoxy propanes.
8. catalytic component according to claim 1, which is characterized in that in the catalytic component, the content of magnesium is 10- 30wt%, the content of titanium are 1-5wt%, and the content of general formula (I) compound represented is 1-20wt%, two shown in general formula (II) The content of ether compound is 1-20wt%.
9. catalytic component according to claim 1, which is characterized in that the precipitation agent is selected from metal halide.
10. catalytic component according to claim 1, which is characterized in that the precipitation agent is halogenated titanium.
11. catalytic component according to claim 1, which is characterized in that the precipitation agent is titanium tetrachloride.
12. a kind of catalyst for olefinic polyreaction, it includes the reaction products of following components:
A. the catalytic component described in any one of claim 1~11;
B. alkyl aluminum compound;
C. optionally, external electron donor component.
13. catalyst according to claim 12, which is characterized in that the alkyl aluminum compound is general formula AlRnX3-nIt is shown Alkyl aluminum compound, R is hydrogen or C in formula1-C20Alkyl, X is halogen, 0 n≤3 <.
14. catalyst according to claim 12, which is characterized in that external electron donor component is general formula (R2)kSi (OR3)4-kShown in organo-silicon compound, 0≤k≤3, R in formula2Selected from halogen, hydrogen atom and C1-C20Alkyl, naphthenic base, virtue Base, halogenated alkyl or amino, R3For C1-C20Alkyl, naphthenic base, aryl, halogenated alkyl or amino.
15. according to the catalyst described in any one of claim 12-14, which is characterized in that the component a) and component b) Molar ratio with titanium:Aluminium is calculated as 1:(5-1000);The molar ratio of the component c) and component a) is with external electron donor:Titanium is calculated as 0- 500:1。
16. catalyst according to claim 15, which is characterized in that the molar ratio of the component a) and component b) is with titanium: Aluminium is calculated as 1:(25-100);The molar ratio of the component c) and component a) is with external electron donor:Titanium is calculated as 25-100:1.
17. a kind of pre-polymerized catalyst for olefinic polymerization, the pre-polymerized catalyst include it is a kind of according to claim 1~ Catalyst described in any one of catalytic component or claim 12-16 described in any one of 11 carries out pre-polymerization with alkene The prepolymer of gained is closed, pre-polymerization multiple is 0.1~1000g olefin polymers/g ingredients of solid catalyst.
18. a kind of method of olefinic polymerization, catalytic component of the alkene described in any one of claim 1~11, power Profit requires to carry out in the presence of the pre-polymerized catalyst described in catalyst or claim 17 described in any one of 12-16.
19. according to the method for claim 18, which is characterized in that the general formula of the alkene is CH2=CHR, wherein R are hydrogen Or C1-C12Alkyl or aryl group.
20. according to the method for claim 19, which is characterized in that the alkene is ethylene or propylene.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699814B2 (en) * 1998-11-04 2004-03-02 Basell Poliolefine Italia S.P.A. Catalysts for the polymerization of olefins
CN1653092A (en) * 2002-05-10 2005-08-10 出光兴产株式会社 Solid catalyst component for olefin polymerization, catalyst for olefin polymerization, and process for producing olefin polymer
CN1958621A (en) * 2005-10-31 2007-05-09 中国石油化工股份有限公司 Solid catalyst component for olefin polymerization, catalyst and catalyst application thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699814B2 (en) * 1998-11-04 2004-03-02 Basell Poliolefine Italia S.P.A. Catalysts for the polymerization of olefins
CN1653092A (en) * 2002-05-10 2005-08-10 出光兴产株式会社 Solid catalyst component for olefin polymerization, catalyst for olefin polymerization, and process for producing olefin polymer
CN1958621A (en) * 2005-10-31 2007-05-09 中国石油化工股份有限公司 Solid catalyst component for olefin polymerization, catalyst and catalyst application thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
醇镁体系聚丙烯催化剂制备技术进展;徐秀东等;《化工进展》;20111231;第30卷(第1期);全文 *

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