CN1310962C - Catalyst component for olefin polymerization reaction and catalyst - Google Patents
Catalyst component for olefin polymerization reaction and catalyst Download PDFInfo
- Publication number
- CN1310962C CN1310962C CNB031405657A CN03140565A CN1310962C CN 1310962 C CN1310962 C CN 1310962C CN B031405657 A CNB031405657 A CN B031405657A CN 03140565 A CN03140565 A CN 03140565A CN 1310962 C CN1310962 C CN 1310962C
- Authority
- CN
- China
- Prior art keywords
- group
- hydrogen
- phenyl
- general formula
- catalyst component
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Abstract
The present invention provides a catalyst component for CH2=CHR olefin polymerization reaction, wherein R is hydrogen or an alkyl group or an aryl group of C1 to C6. The catalyst component comprises magnesium, titanium, halogen and an electron donor, wherein the electron donor is selected from at least one glycol ester compound; R1 to R12 can be the same or different and are hydrogen or straight chain or branched chain alkyl groups of C1 to C10, naphthenic groups of C3 to C10, aryl groups of C6 to C10, and alkaryl groups or aralkyl groups of C7 to C10, but R1 to R12 are not hydrogen simultaneously; two or more than groups in R1 to R12 can be mutually bonded to generate one or a plurality of condensed ring structures; R13 and R14 can be the same or different and represent the straight chain or branched chain alkyl group of C1 to C10, a naphthenic group of C3 to C20, the aryl group of C6 to C10, an alkaryl group of C7 to C20 or an aralkyl group of C7 to C20. Hydrogen on a benzene ring in the aryl group or the alkaryl group or the aralkyl group can be optionally replaced by a halogen atom.
Description
Technical field
The present invention relates to ingredient of solid catalyst of a kind of diol ester compound that contains special construction and preparation method thereof, contain the catalyzer of this ingredient of solid catalyst and this catalyzer at CH
2Application in the=CHR olefinic polyreaction, wherein R is hydrogen or C
1-C
6Alkyl or aryl, special application in propylene polymerization can obtain the polymkeric substance of high yield, high isotactic and molecular weight distribution broad.
Technical background
As everyone knows, with magnesium, titanium, halogen and electron donor solid titanium catalyst component, can be used for CH as basal component
2=CHR olefinic polyreaction, particularly in alpha-olefine polymerizing, can obtain the polymkeric substance of higher yields and higher tacticity with 3 carbon or more carbon atoms, wherein the electron donor compound is one of requisite composition in the catalyst component, and along with the development of internal electron donor compound has caused polyolefin catalyst constantly to update.At present, multiple electron donor compound is disclosed in a large number, for example polycarboxylic acid, monocarboxylic ester or multi-carboxylate, acid anhydrides, ketone, monoether or polyether, alcohol, amine etc. and derivative thereof, wherein comparatively commonly used is aromatic carboxylates's class of binary, for example n-butyl phthalate or diisobutyl phthalate etc. can be referring to Chinese patent CN85100997A.
In recent years, the electron donor that people attempt to adopt other compound to be used as in the olefin polymerization catalyst components again uses, for example at Chinese patent CN1042547A and the disclosed catalyst component that is used for olefinic polyreaction of CN1143651A, special 1 of two ether groups that contain have been adopted, the 3-diether compound is as electron donor, 2-sec.-propyl-2-isopentyl-1 for example, 3-Propanal dimethyl acetal, 2,2-diisobutyl-1,3-Propanal dimethyl acetal and 9,9-two (methoxymethyl) fluorenes etc.At the disclosed ingredient of solid catalyst that is used for olefinic polyreaction of Chinese patent CN1054139A, adopted special 1 of two ketone groups that contain, the 3-cyclohexadione compounds is as electron donor, for example 2,2,4,6,6-pentamethyl--3,5-heptadione and 2,2,6,6-tetramethyl--4-3,5-heptadione etc.
The special dibasic aliphatic carboxylic acid ester compound of one class is disclosed again recently, as (referring to CN1313869A, CN1236373A and CN1236374A) such as succinate, malonic ester, glutarates, the use of this class electron donor compound not only can improve activity of such catalysts, and the molecular weight distribution of gained propene polymer is obviously widened.
Yet, the aromatic carboxylic acid ester compound of the above-mentioned disclosed binary of above-mentioned employing, contain 1 of two ether groups, the catalyzer that is used for olefinic polymerization of 3-diether compound and the preparation of dibasic aliphatic carboxylic acid ester compound all exists certain defective in actual applications, for example adopt the catalytic activity of catalyzer of aromatic carboxylic acid ester compound of binary lower, and the molecular weight distribution of resulting polymers is also narrower; Adopt 1, though the catalyzer of 3-diether compound is active higher, and catalyzer susceptibility that hydrogen is transferred might as well, the narrow molecular weight distribution of resulting polymers is unfavorable for the exploitation of the different trades mark of polymkeric substance; And adopt the hydrogen response of catalyzer of recent disclosed dibasic aliphatic carboxylicesters relatively poor.
The inventor unexpectedly finds, in olefin polymerization catalysis by using a kind of new diol ester compound that contains special construction as electron donor, can obtain the catalyzer of high comprehensive performance, when being used for propylene polymerization, can obtain gratifying polymerization yield rate, and the stereospecificity of polymkeric substance is higher, catalyzer is also fine to the susceptibility of hydrogen accent simultaneously, the molecular weight distribution broad of resulting polymers helps the exploitation of the different trades mark of polymkeric substance.
Summary of the invention
One of purpose of the present invention is to provide a kind of CH of being used for
2The catalyst component of=CHR olefinic polyreaction, wherein R is hydrogen or C
1-C
6Alkyl or aryl, this catalyst component comprises magnesium, titanium, halogen and electron donor, this electron donor is selected from least a diol ester compound in the following general formula (I):
R wherein
1-R
12Can be identical or inequality, be hydrogen or C
1-C
10The alkyl of straight or branched, C
3-C
10Cycloalkyl, C
6-C
10Aryl, C
7-C
10Alkaryl or aralkyl, but R
1-R
12Be not hydrogen simultaneously; R
1-R
12In two or more groups mutually bonding generate one or several condensed ring structure;
R
13And R
14Can be identical or inequality, represent C
1-C
10Straight or branched alkyl, C
3-C
20Cycloalkyl, C
6-C
20Aryl, C
7-C
20Alkaryl or C
7-C
20Aryl, the benzene ring hydrogen can randomly be replaced by halogen atom in described aryl or alkaryl or the aryl.
In above-mentioned diol ester general formula compound, preferred R
1And R
2, R
11And R
12In to have a group respectively at least be hydrogen.
In above-mentioned diol ester general formula compound, also preferred R
3-R
10In to have a group at least be not hydrogen.More preferably, R
3-R
10In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl.Further preferred, R
5-R
8In to have a group at least be not hydrogen; More preferably, R
5-R
8In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl.Also further preferred R
5And R
6, R
7And R
8In to have a group respectively at least be not hydrogen; More preferably R
5And R
6, R
7And R
8In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl respectively.
In above-mentioned diol ester general formula compound, preferred R
13And R
14Group is selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, amyl group, cyclopentyl, cyclohexyl, phenyl, halogenated phenyl, alkyl phenyl, halogenated alkyl phenyl, indenyl, benzyl or phenylethyl; More preferably, R
13And R
14Group has at least one to be selected from phenyl, halogenated phenyl, alkyl phenyl or halogenated alkyl phenyl; Further preferably, R
13And R
14Group all is selected from phenyl, halogenated phenyl, alkyl phenyl or halogenated alkyl phenyl.
The particular compound of general formula (I) can be selected from:
1,4-xylyl alcohol dibenzoate, 2,5-phenylbenzene-1,6-heptanediol dibenzoate, 2,2 '-biphenyl dimethanol dibenzoate, 2,2 '-biphenyl dimethanol dipropionate, 2,2 '-biphenyl dimethanol two pivalates, 2,2 '-dinaphthalene dimethanol dibenzoate, 2,2 '-methylene bridge binaphthol dibenzoate, 2,3-dimethyl-1,6-hexylene glycol dibenzoate, 2,4-dimethyl-1,6-hexylene glycol dibenzoate, 3,4-dibutyl-1,6-hexylene glycol dibenzoate, 3,3 '-dibutyl-1,6-hexylene glycol dibenzoate, 3,3 '-dimethyl-1,6-hexylene glycol dibenzoate, 2,2 '-dimethyl-1,6-hexylene glycol dibenzoate, 2,5-dibutyl-1,6-hexylene glycol dibenzoate, 3,4-dimethyl-1,6-hexylene glycol dibenzoate, 3,5-dimethyl-1,6-hexylene glycol dibenzoate, 2,5-dimethyl-1,6-hexylene glycol dibenzoate, 2,3,4,5-tetramethyl--1,6-hexylene glycol dibenzoate, 2,5-phenylbenzene-1,6-hexylene glycol dibenzoate, 2,7-ethohexadiol dibenzoate, 3,4-dibutyl-2,7-ethohexadiol dibenzoate, 3,3 '-dibutyl-2,7-ethohexadiol dibenzoate, 3,3 '-dimethyl-2,7-ethohexadiol dibenzoate, 4,4 '-dimethyl-2,7-ethohexadiol dibenzoate, 4,4 '-dibutyl-2,7-ethohexadiol dibenzoate, 3,5-dibutyl-2,7-ethohexadiol dibenzoate, 3,6-dimethyl-2,7-ethohexadiol dibenzoate, 3,4-dimethyl-2,7-ethohexadiol dibenzoate, 3,5-dimethyl-2,7-ethohexadiol dibenzoate, 3,3 ', 4,4 '-tetramethyl--2,7-ethohexadiol dibenzoate, 3,3 ', 5,5 '-tetramethyl--2,7-ethohexadiol dibenzoate, 3,3 ', 6,6 '-tetramethyl--2,7-ethohexadiol dibenzoate, 3,4,5,6-tetramethyl--2,7-ethohexadiol dibenzoate, 3,3 ', 4,4 ', 5,5 ', 6,6 '-prestox-2,7-ethohexadiol dibenzoate, 3,5-phenylbenzene-2,7-ethohexadiol dibenzoate, 3,4-phenylbenzene-2,7-ethohexadiol dibenzoate, 3,6-phenylbenzene-2,7-ethohexadiol dibenzoate, 3,4-diethyl-1,6-hexylene glycol dibenzoate, 3,4-dipropyl-1,6-hexylene glycol dibenzoate, 3,4-di-isopropyl-1, oneself two glycol dibenzoates of 6-, 3,4-di-n-butyl-1,6-hexylene glycol dibenzoate, 3,4-di-t-butyl-1, oneself two glycol dibenzoates of 6-, 3,4-phenylbenzene-1,6-hexylene glycol dibenzoate, 5,6-dimethyl-2,7-ethohexadiol dibenzoate, 5,6-diethyl-2,7-ethohexadiol dibenzoate, 5,6-dipropyl-2,7-ethohexadiol dibenzoate, 5,6-di-isopropyl-2,7-ethohexadiol dibenzoate, 3,6-di-n-butyl-2,7-ethohexadiol dibenzoate, 3,6-di-t-butyl-2,7-ethohexadiol dibenzoate, 3,6-phenylbenzene-2,7-ethohexadiol dibenzoate, 3,6-dibenzyl-2,7～ethohexadiol dibenzoate.
Above-mentioned dibasic alcohol ester compound can be synthetic by various reactions, wherein can make corresponding dibasic alcohol carry out esterification and obtain corresponding binary alcohol esters in the presence of corresponding acid or acyl chlorides.The synthetic of relevant dibasic alcohol can be referring to the document of prior art, as referring to Acta Chemica Scandina-vica21, and 1967, pp.718-720 also can be referring to the preparation method of disclosed dibasic alcohol among the Chinese patent CN1141285A.
The ingredient of solid catalyst that is used for olefinic polymerization of the present invention preferably comprises titanium compound, magnesium compound and is selected from the have general formula reaction product of diol ester compound of (I).
Wherein used magnesium compound is selected from a kind of by in-oxyl or the halo-oxyl institute metathetical derivative of one of them halogen atom in the hydrate of magnesium dihalide, alkoxyl magnesium, alkyl magnesium, magnesium dihalide or alcohol adduct and the magnesium dihalide molecular formula, or their mixture.The alcohol adduct of preferred magnesium dihalide or magnesium dihalide, for example magnesium dichloride, dibrominated magnesium, two magnesium iodides and their alcohol adduct.
It is TiX that wherein used titanium compound can be selected general formula for use
n(OR)
4-nCompound, R is that carbonatoms is 1～20 alkyl in the formula, X is a halogen, n=1～4.For example: titanium tetrachloride, titanium tetrabromide, titanium tetra iodide, four titanium butoxide, purity titanium tetraethoxide, a chlorine triethoxy titanium, dichloro diethoxy titanium, trichlorine one ethanolato-titanium, preferred titanium tetrachloride.
What particularly point out is magnesium compound, preferably is dissolved in the solvent system that contains organic epoxy compounds and organo phosphorous compounds.Wherein organic epoxy compounds comprises at least a in oxide compound, glycidyl ether and the inner ether of 2～8 aliphatics alkene, diolefine or halogenated aliphatic alkene or diolefine of carbonatoms.Particular compound is as oxyethane, propylene oxide, butylene oxide ring, butadiene oxide, butadiene double oxide, epoxy chloropropane, methyl glycidyl ether, diglycidylether, tetrahydrofuran (THF).
Wherein organo phosphorous compounds comprises the hydrocarbyl carbonate or the halo hydrocarbyl carbonate of ortho-phosphoric acid or phosphorous acid, concrete as: ortho-phosphoric acid trimethyl, ortho-phosphoric acid triethyl, ortho-phosphoric acid tri-n-butyl, ortho-phosphoric acid triphenylmethyl methacrylate, trimethyl phosphite, triethyl-phosphite, tributyl phosphate, tricresyl phosphite benzene methyl.
Can select to press the method for stating and prepare ingredient of solid catalyst of the present invention.
At first, magnesium compound is dissolved in the solvent system of being made up of organic epoxy compounds, organo phosphorous compounds and inert diluent, mixes with titanium compound behind the formation homogeneous solution, in the presence of precipitation additive, separate out solids; This solids by using is selected from the diol ester compound compound of general formula (I) and handles, it is attached on the solids, in case of necessity, with titanium tetrahalide and inert diluent solids is handled again, wherein precipitation additive is a kind of in organic acid anhydride, organic acid, ether, the ketone, or their mixture.Concrete as: diacetyl oxide, Tetra hydro Phthalic anhydride, Succinic anhydried, MALEIC ANHYDRIDE, pyromellitic acid anhydride, acetic acid, propionic acid, butyric acid, vinylformic acid, methacrylic acid, acetone, methylethylketone, benzophenone, methyl ether, ether, propyl ether, butyl ether, amyl ether.
Described each component is in every mole of magnesium halide, and organic epoxy compounds is 0.2～10 mole, and organo phosphorous compounds is 0.1～3 mole, and precipitation additive is 0～1.0 mole, and titanium compound is 0.5～150 mole, and general formula diol ester compound is 0.02～0.4 mole.
According to another kind of method, be to be TiX with general formula
n(OR)
4-nTitanium compound, R is that carbonatoms is 1～20 alkyl in the formula, X is a halogen, n=1～4, preferred TiCl
4, with general formula be MgCl
2The adducts of pROH reacts and the preparation ingredient of solid catalyst.At MgCl
2Among the pROH, p is 0.1 to 6 number, and is preferred 2 to 3.5, and R is the alkyl with 1-18 carbon atom.Adducts can be made spherical by the following method aptly: not with the miscible unreactive hydrocarbons of adducts in the presence of, pure and mild magnesium chloride is mixed, make the rapid chilling of this emulsion, thereby adducts solidified with the form of spheroidal particle.The adducts that so obtains can be directly and the titanium compound reaction, perhaps it can pass through the dealcoholization (80-130 ℃) of thermal control to obtain a kind of adducts in advance before reacting with titanium compound, wherein Chun mole number generally is lower than 3, preferably between 0.1 and 2.7.Can be by adducts (dealcoholysis or itself) be suspended in cold TiCl
4In (general 0 ℃), and with the mixture temperature programming to 80-130 ℃ and under this temperature, kept 0.1-2 hour, carry out reaction with titanium compound.TiCl
4Processing can be carried out once or repeatedly.Using TiCl
4Can add the above-mentioned dibasic alcohol ester compound of general formula the present invention during the processing and handle, this processing also can repeat once or repeatedly.
Another object of the present invention is to provide a kind of CH of being used for
2The catalyzer of=CHR olefinic polyreaction, wherein R is hydrogen or C
1-C
6Alkyl or aryl, comprise the reaction product of following component:
(1) a kind of above-mentioned diol ester compound that contains magnesium, titanium, halogen and be selected from general formula (I): ingredient of solid catalyst;
(2) alkylaluminium cpd;
(3) randomly, external electron donor component.
Wherein alkylaluminium cpd is that general formula is AlR
nX
3-nCompound, R is a hydrogen in the formula, carbonatoms is 1～20 alkyl, X is a halogen, n is the number of 1＜n≤3; Specifically can be selected from triethyl aluminum, tri-propyl aluminum, three n-butylaluminum, triisobutyl aluminium, tri-n-octylaluminium, triisobutyl aluminium, a hydrogen diethyl aluminum, a hydrogen diisobutyl aluminum, aluminium diethyl monochloride, a chloro-di-isobutyl aluminum, sesquialter ethyl aluminum chloride, ethyl aluminum dichloride, preferred triethyl aluminum, triisobutyl aluminium.
When needing the very high olefin polymer of taxis to use, need to add (3) external electron donor compound, for example general formula is R
nSi (OR)
4-nSilicoorganic compound, 0≤n in the formula≤3, R and R
*Be of the same race or different alkyl, cycloalkyl, aryl, haloalkyl, amido, R also can be halogen or hydrogen atom.For example: trimethylammonium methoxy silane, trimethylethoxysilane, dimethyldimethoxysil,ne, dimethyldiethoxysilane, dimethoxydiphenylsilane, phenylbenzene diethoxy silane, phenyl triethoxysilane, phenyltrimethoxysila,e, vinyltrimethoxy silane, cyclohexyl methyl dimethoxy silane, methyl-t-butyldimethoxysilane, preferred cyclohexyl methyl dimethoxy silane, dimethoxydiphenylsilane.
The ratio between component (1), component (2) and the component (3) wherein, with titanium: aluminium: the molar ratio computing between the silicon is 1: 5～1000: 0～500; Be preferably 1: 25～100: 25～100.
Above-mentioned external electron donor component also can be selected from monobasic or polybasic organic acid ester, for example monobasic or polybasic benzoates.Preferred monobasic benzoates.
1 of the also optional self-drifting of above-mentioned external electron donor component (II), 3-two ethers:
R wherein
I, R
II, R
III, R
IV, R
VAnd R
VIIdentical or different, for hydrogen or have the hydrocarbyl group of 1 to 18 carbon atom, and R
VIIAnd R
VIIICan be identical or different, for having the hydrocarbyl group of 1 to 18 carbon atom; R
I-R
VIIIGroup in one or morely can link up into ring.Preferably, R
VIIAnd R
VIIIBe selected from C
1-C
4Alkyl group, R
IIIAnd R
IVForm undersaturated condensed ring, and R
I, R
II, R
V, and R
VIBe hydrogen.For example: 9, two (methoxymethyl) fluorenes of 9-.
The present invention also provides a kind of alkene CH that is used for
2=CHR polymeric method, wherein R is the hydrocarbyl group of hydrogen or 1-12 carbon atom, described polymerization side carries out in the presence of above-mentioned catalyzer or pre-polymerized catalyst.Olefinic polyreaction of the present invention carries out according to known polymerization process, can carry out in liquid phase or gas phase, perhaps also can carry out under the operation of liquid and gas polymerization stage combination.Adopt conventional technology such as slurry process, gas-phase fluidized-bed etc., wherein alkene is selected from ethene, propylene, 1-butylene, 4-methyl-1-pentene and 1-hexene, the equal polymerization of special propylene with or the copolymerization of other alkene of propylene.Be to adopt following reaction conditions preferably:
Polymerization temperature: 0～150 ℃, preferred 60～90 ℃.
Catalyzer of the present invention can directly add and be used for polymerization process in the reactor.Perhaps, catalyzer can carry out prepolymerization before adding first polymerization reactor.In the present invention, term " pre-polymerized catalyst " means with the catalyzer of low transforming degree through polymerization procedure.According to the present invention, described pre-polymerized catalyst comprises the prepolymer that above-mentioned ingredient of solid catalyst and alkene carry out the prepolymerization gained, and the pre-polymerization multiple is 0.1-1000g olefin polymer/g ingredient of solid catalyst.
Can adopt the alpha-olefin identical to carry out prepolymerization, wherein carry out prepolymerized alkene and be preferably ethene or propylene with aforementioned alkene.Specifically, particularly preferably be, the mixture that adopts ethene or itself and amount to be up to one or more alpha-olefins of 20mol% carries out prepolymerization.Preferably, the transforming degree of pre-polymerized catalyst components is that about 0.2 gram is to about 500 gram polymkeric substance/gram ingredients of solid catalyst.
The prepolymerization operation can under preferred 0 to the 50 ℃ temperature, be carried out in liquid or in the gas phase at-20 to 80 ℃.Prepolymerization step can be used as online the carrying out of a part in the continuous polymerization technique, or carries out independently in periodical operation.For preparation amount is the polymkeric substance of 0.5-20g/g catalyst component, the batch pre-polymerization of preferred especially catalyzer of the present invention and ethene.Polymerization pressure is 0.01-10MPa.
Catalyzer of the present invention also is applicable to produces polyethylene and ethene and alpha-olefin, as the multipolymer of propylene, butylene, amylene, hexene, octene, 4-methylpentene-1.
It is worthy of note that the present invention is by adopting novel internal electron donor diol ester compound, can obtain the catalyzer of high comprehensive performance, when being used for propylene polymerization, can obtain gratifying polymerization yield rate, and the stereospecificity of polymkeric substance is higher, catalyzer is also fine to the susceptibility of hydrogen accent simultaneously, and the molecular weight distribution broad of resulting polymers helps the exploitation of the different trades mark of polymkeric substance.
Embodiment: compound synthetic
Embodiment 1
1, the preparation of 4-xylyl alcohol dibenzoate
0.03mol 1, add 30ml tetrahydrofuran (THF) and 0.09mol pyridine in the 4-xylyl alcohol, under agitation add the 0.075mol Benzoyl chloride, reflux 4h.The cooling back adds 20ml saturated aqueous common salt, ethyl acetate extraction, anhydrous Na
2SO
4Drying is removed and is desolvated.Use ethyl acetate: sherwood oil (1: 1) recrystallization gets white solid 1,4-xylyl alcohol dibenzoate.Yield 95%, mp84～85 ℃.
1,4-xylyl alcohol dibenzoate
1H NMR (TMS, CDCl
3, ppm, δ): 5.3 (4H, s, the methylene radical H of ester group), 7.4～8.1 (10H, m, phenyl ring H).
Embodiment 2
2,2 '-preparation of biphenyl dimethanol dibenzoate
(1) 2,2 '-preparation of biphenyl dicarboxylic acid diethyl alcohol ester
0.1mol 2,2 '-adding 0.3mol ethanol, 40ml toluene and the 0.4ml vitriol oil in the biphenyl dicarboxylic acid acid anhydride, the stirring and evenly mixing post-heating refluxes.Dewater with water trap, reach Theoretical Calculation amount, stopped reaction up to the water of telling.With the saturated sodium carbonate solution neutralization, ethyl acetate extraction is told upper solution, and the saturated common salt aqueous solution is washed till neutrality, anhydrous sodium sulfate drying.Remove and to desolvate, underpressure distillation get colourless liquid 2,2 '-biphenyl dicarboxylic acid diethyl alcohol ester, yield 90%.
(2) 2,2 '-preparation of biphenyl dimethanol
Add the 100ml anhydrous diethyl ether in the 3g Lithium Aluminium Hydride, the ice bath cooling is vigorous stirring down.Slowly drip 0.05mol 2,2 '-biphenyl dicarboxylic acid diethyl alcohol ester, reflux 5h then.The Lithium Aluminium Hydride of cooling back water decomposing excessive filters back extracted with diethyl ether solution, anhydrous sodium sulfate drying.Remove and to desolvate, column chromatography get white solid 2,2 '-the biphenyl dimethanol, yield 75%.M.p.98～103 ℃, the IR spectrogram is at 3400cm
-1There is strong absorption peak at the place, and at 1700cm
-1About do not have absorption peak, prove that reduction reaction carries out fully.
(3) 2,2 '-preparation of biphenyl dimethanol dibenzoate
0.03mol 2,2 '-add 30ml tetrahydrofuran (THF) and 0.09mol pyridine in the biphenyl dimethanol, under agitation add the 0.075mol Benzoyl chloride, reflux 4h.The cooling back adds 20ml saturated aqueous common salt, ethyl acetate extraction, anhydrous Na
2SO
4Drying is removed and is desolvated.Column chromatography, colourless viscous liquid 2,2 '-biphenyl dimethanol dibenzoate, yield 93%.
2,2 '-biphenyl dimethanol dibenzoate
1H NMR (TMS, CDCl
3, ppm,): 5.16 (4H, s, the methylene radical H of ester group), 7.2～8.2 (18H, m, phenyl ring H).
Embodiment 3
3,4-dibutyl-1,6-hexylene glycol dibenzoate
In reactor, add 3,4-dibutyl-1,6-hexylene glycol 4.4g, Benzoyl chloride 3.8g, pyridine 4.0g and tetrahydrofuran (THF) 70ml mix, and are heated to backflow.After occurring refluxing, kept 4 hours.Reduce to room temperature then, in reaction system, add water till inorganic mutually transparent.Tell organic phase, merge with organic phase with the inorganic back mutually of extracted with diethyl ether.After washing organic phase with water, with the organic phase drying, after concentrating, isolate product, obtain the 4.3g product with anhydrous sodium sulphate.3,4-dibutyl-1,6-hexylene glycol dibenzoate
1HNMR (TMS, CDCl
3, ppm, δ): 0.8～1.6 (18H), 2.1～2.3 (6H), 4.3～4.5 (4H), 7.4～8.1 (10H).
Embodiment 4
2,2 '-dinaphthalene dimethanol dibenzoate
In reactor, add dinaphthalene diphenol 4.3g, Benzoyl chloride 4g, pyridine 4.5g and tetrahydrofuran (THF) 70ml mix, and are heated to backflow.After occurring refluxing, kept 4 hours.Reduce to room temperature then, in reaction system, add water till inorganic mutually transparent.Tell organic phase, merge with organic phase with the inorganic back mutually of extracted with diethyl ether.After washing organic phase with water, with the organic phase drying, after concentrating, isolate product, obtain the 8.2g product with anhydrous sodium sulphate.2,2 '-dinaphthalene dimethanol dibenzoate
1H NMR (TMS, CDCl
3, ppm, δ): 4.8 (4H), 7.0～8.1 (22H).
The preparation of catalyst component:
(1) preparation of olefins polymerizing solid catalyst component
In through the abundant metathetical reactor of high pure nitrogen, add magnesium chloride 4.8g successively, toluene 95ml, epoxy chloropropane 4ml, tributyl phosphate (TBP) 12.5ml is warming up to 50 ℃ under stirring, and kept 2.5 hours, solid dissolves fully, adds Tetra hydro Phthalic anhydride 1.4g, continues to keep 1 hour.Solution is cooled to below-25 ℃, drips TiCl in 1 hour
456ml slowly is warming up to 80 ℃, separates out solids in temperature-rise period gradually, adds the resulting compound 6mmol of the foregoing description respectively, and holding temperature 1 hour after the filtration, adds toluene 70ml, and the washing secondary obtains solid sediment.Add toluene 60ml then, TiCl
440ml is warmed up to 100 ℃, handles two hours, after the venting filtrate, adds toluene 60ml again, TiCl
440ml is warmed up to 100 ℃, handles venting filtrate two hours.Add toluene 60ml, boiling attitude washing three times adds hexane 60ml again, and boiling attitude washed twice adds hexane 60ml, after the normal temperature washed twice, obtains ingredient of solid catalyst.
(2) propylene polymerization experiment
The catalyst component of above-mentioned gained is carried out propylene polymerization respectively.The propylene polymerization program is: volume is the stainless steel cauldron of 5L, after gaseous propylene is fully replaced, adds AlEt
32.5mmol methylcyclohexyl dimethoxy silane (CHMMS) 0.1mmol adds about 8mg of ingredient of solid catalyst and 1.2L hydrogen that the foregoing description obtains again, feeds liquid propene 2.3L, is warming up to 70 ℃, keeps this temperature 1 hour.Cooling, pressure release obtains the PP powder.Polymerization result such as table 1.
Comparative Examples 1:
The preparation of catalyst component:
With embodiment 1, only electron donor is replaced with unsubstituted 1,6-hexylene glycol dibenzoate.
Comparative Examples 2:
The preparation of catalyst component:
With embodiment 1, only electron donor is replaced with diisobutyl phthalate
Propylene polymerization: with embodiment 1.
Table 1
| Active (kgPP/gcat) | Degree of isotacticity (%) | Molecular weight distribution | Melting index g/10min | |
| Embodiment 1 | 10.6 | 96.1 | 7.2 | 5.7 |
| Embodiment 2 | 16.3 | 92.8 | 6.7 | 4.0 |
| Embodiment 3 | 30.6 | 97.0 | 7.5 | 1.9 |
| Embodiment 4 | 10.1 | 95.4 | 6.6 | 2.4 |
| Comparative Examples 1 | 6.3 | 94.9 | / | 1.9 |
| Comparative Examples 2 | / | / | 4.3 | 3.0 |
From last table 1 more as can be seen, the catalyzer that to adopt diol ester compound of the present invention be internal electron donor is than adopting unsubstituted diol ester compound, activity of such catalysts obviously improves, directional property also can improve, and than now commonly used be that the molecular weight distribution of the prepared polymkeric substance of the catalyzer of internal electron donor is obviously widened with the phthalic acid.
Claims (25)
1, the catalyst component that is used for olefinic polymerization, it comprises magnesium, titanium, halogen and electron donor, and this electron donor is selected from least a diol ester compound in the following general formula (I):
R wherein
1-R
12Can be identical or inequality, be hydrogen or C
1-C
10The alkyl of straight or branched, C
3-C
10Cycloalkyl, C
6-C
10Aryl, C
7-C
10Alkaryl or aralkyl, but R
1-R
12Be not hydrogen simultaneously; R
1-R
12In two or more groups mutually bonding generate one or several condensed ring structure;
R
13And R
14Can be identical or inequality, represent C
1-C
10Straight or branched alkyl, C
3-C
20Cycloalkyl, C
6-C
20Aryl, C
7-C
20Alkaryl or C
7-C
20Aryl, the benzene ring hydrogen can randomly be replaced by halogen atom in described aryl or alkaryl or the aryl.
2, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
1And R
2, R
11And R
12In to have a group respectively at least be hydrogen.
3, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
3-R
10In to have a group at least be not hydrogen.
4, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
3-R
10In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl.
5, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
5-R
8In to have a group at least be not hydrogen.
6, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
5-R
8In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl.
7, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
5And R
6, R
7And R
8In to have a group respectively at least be not hydrogen.
8, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), R
5And R
6, R
7And R
8In have at least a group to be selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, phenyl or halogenated phenyl respectively.
9, the catalyst component that is used for olefinic polyreaction according to claim 1, in the diol ester compound of wherein said general formula (I), described R
13And R
14Group is selected from methyl, ethyl, propyl group, sec.-propyl, butyl, the tertiary butyl, amyl group, cyclopentyl, cyclohexyl, phenyl, halogenated phenyl, alkyl phenyl, halogenated alkyl phenyl, indenyl, benzyl or phenylethyl.
10, the catalyst component that is used for olefinic polyreaction according to claim 9, in the diol ester compound of wherein said general formula (I), described R
13And R
14Group has at least one to be selected from phenyl, halogenated phenyl, alkyl phenyl or halogenated alkyl phenyl.
11, the catalyst component that is used for olefinic polyreaction according to claim 9, in the diol ester compound of wherein said general formula (I), described R
13And R
14Group all is selected from phenyl, halogenated phenyl, alkyl phenyl or halogenated alkyl phenyl.
12, according to the described catalyst component that is used for olefinic polymerization of one of claim 1-11, it comprises titanium compound, magnesium compound and is selected from the reaction product of the diol ester compound of general formula (I),
Magnesium compound is selected from a kind of in one of them halogen atom alkoxy in the hydrate of magnesium dihalide, alkoxyl magnesium, alkyl magnesium, magnesium dihalide or alcohol adduct and the magnesium dihalide molecular formula or the halogenated alkoxy institute metathetical derivative or their mixture;
Titanium compound is that general formula is TiXn (OR)
4-n, R is that carbonatoms is 1～20 alkyl in the formula, X is a halogen, n=1～4.
13, the catalyst component that is used for olefinic polymerization according to claim 12, the magnesium compound that it adopted is dissolved in the solvent system that contains organic epoxy compounds and organo phosphorous compounds.
14, the catalyst component that is used for olefinic polymerization according to claim 13, its organic epoxy compounds comprise at least a in oxide compound, glycidyl ether and the inner ether of 2～8 aliphatics alkene, diolefine or halogenated aliphatic alkene or diolefine of carbonatoms.
15, the catalyst component that is used for olefinic polymerization according to claim 13, its organo phosphorous compounds are the hydrocarbyl carbonate or the halo hydrocarbyl carbonate of ortho-phosphoric acid or phosphorous acid.
16, the catalyst component that is used for olefinic polymerization according to claim 12, the magnesium compound that it adopted is the alcohol adduct of magnesium dihalide.
17, a kind of CH that is used for
2The catalyzer of=CHR olefinic polyreaction, wherein R is hydrogen or C
1-C
6Alkyl or aryl, comprise the reaction product of following component:
(1) the described catalyst component of one of claim 1-16;
(2) alkylaluminium cpd;
(3) randomly, external electron donor component.
18, catalyzer according to claim 17, wherein external electron donor component general formula is R
nSi (OR)
4-nThe external electron donor compound, 0≤n in the formula≤3, R and R
*Be of the same race or different alkyl, cycloalkyl, aryl, haloalkyl, amido, R also can be halogen or hydrogen atom.
19, catalyzer according to claim 17, wherein the external electron donor component is selected from monobasic or polybasic organic acid ester.
20, catalyzer according to claim 17, wherein the external electron donor component is selected from monobasic or polybasic benzoates.
21, catalyzer according to claim 17, wherein the external electron donor component is selected from 1 of general formula (II), 3-two ethers:
R wherein
I, R
II, R
III, R
IV, R
VAnd R
VIIdentical or different, for hydrogen or have the hydrocarbyl group of 1 to 18 carbon atom, and R
VIIAnd R
VIIICan be identical or different, for having the hydrocarbyl group of 1 to 18 carbon atom; R
I-R
VIIIGroup in one or morely can link up into ring.
22, the catalyzer of claim 21, described 1, R in the general formula of 3-diether (II)
VIIAnd R
VIIIBe selected from C
1-C
4Alkyl group, R
IIIAnd R
IVForm undersaturated condensed ring, and R
I, R
II, R
V, and R
VIBe hydrogen.
23, a kind of alkene CH that is used for
2=CHR polymeric pre-polymerized catalyst, wherein R is hydrogen or C
1-C
12Alkyl group, described pre-polymerized catalyst comprises and a kind ofly carries out the prepolymer of prepolymerization gained according to each described ingredient of solid catalyst and alkene among the claim 1-16, the pre-polymerization multiple is 0.1-1000g olefin polymer/g ingredient of solid catalyst.
24, the pre-polymerized catalyst of claim 23, wherein carrying out prepolymerized alkene is ethene or propylene.
25, be used for alkene CH
2=CHR polymeric method, wherein R is the hydrocarbyl group of hydrogen or 1-12 carbon atom, carries out in the presence of each described catalyzer or the pre-polymerized catalyst in claim 17-24.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031405657A CN1310962C (en) | 2003-05-30 | 2003-05-30 | Catalyst component for olefin polymerization reaction and catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031405657A CN1310962C (en) | 2003-05-30 | 2003-05-30 | Catalyst component for olefin polymerization reaction and catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1552740A CN1552740A (en) | 2004-12-08 |
| CN1310962C true CN1310962C (en) | 2007-04-18 |
Family
ID=34323826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB031405657A Expired - Lifetime CN1310962C (en) | 2003-05-30 | 2003-05-30 | Catalyst component for olefin polymerization reaction and catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1310962C (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102040690A (en) | 2009-10-20 | 2011-05-04 | 中国石油化工股份有限公司 | Method for preparing polypropylene with low ash content |
| JP5785809B2 (en) * | 2011-07-28 | 2015-09-30 | 東邦チタニウム株式会社 | SOLID CATALYST COMPONENT FOR OLEFIN POLYMERIZATION, PROCESS FOR PRODUCING THE SAME, OLEFIN POLYMERIZATION CATALYST, AND METHOD FOR PRODUCING OLEFIN POLYMER |
| EP3868796A4 (en) | 2018-10-19 | 2022-07-13 | China Petroleum & Chemical Corporation | Catalyst component and catalyst for olefin polymerization, and application thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5360776A (en) * | 1990-11-07 | 1994-11-01 | Neste Oy | Stereoselective catalyst for the polymerization of olefins |
| CN1230552A (en) * | 1998-03-11 | 1999-10-06 | 住友化学工业株式会社 | Solid catalyst component and catalyst for olefin polymerization, and process for producing olefin polymer |
| CN1258683A (en) * | 1998-12-30 | 2000-07-05 | 中国石油化工集团公司 | Catalyst for polymerization or copolymerization of propylene and its preparation and use |
-
2003
- 2003-05-30 CN CNB031405657A patent/CN1310962C/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5360776A (en) * | 1990-11-07 | 1994-11-01 | Neste Oy | Stereoselective catalyst for the polymerization of olefins |
| CN1230552A (en) * | 1998-03-11 | 1999-10-06 | 住友化学工业株式会社 | Solid catalyst component and catalyst for olefin polymerization, and process for producing olefin polymer |
| CN1258683A (en) * | 1998-12-30 | 2000-07-05 | 中国石油化工集团公司 | Catalyst for polymerization or copolymerization of propylene and its preparation and use |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1552740A (en) | 2004-12-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1146585C (en) | Components and catalysts for polymerization of olefins | |
| CN1670043A (en) | Catalyst for polymerization of olefins and its preparation and polymerization method | |
| CN102234337B (en) | Catalyst components for olefin polymerization reaction, and catalyst thereof | |
| CN100348624C (en) | Catalyst components for olefinic polyreaction and catalyst thereof | |
| CN1942488A (en) | Components and catalysts for the polymerization of olefins | |
| CN1831017A (en) | Catalyst for olefin polymerization, prepn. method and polymerization method thereof | |
| CN1137156C (en) | Catalyst for olefine polymerization and its formula and application | |
| CN103665203A (en) | Solid catalyst component for olefinic polymerization and catalyst | |
| CN1887918A (en) | Catalyst for olefin polymerization or copolymerization at high temperature | |
| CN100338103C (en) | Catalyst component for olefinic polymerization and its catalyst | |
| CN101724105B (en) | Catalyzer component for olefin polymerization reaction and catalyzer thereof | |
| CN100429243C (en) | Method for preparing catalyst constituent for olefinic polymerization | |
| CN1097596C (en) | Catalyst to make the isotactic degree of polypropylene easy to regulate, the preparation of its active component and its application | |
| CN1310962C (en) | Catalyst component for olefin polymerization reaction and catalyst | |
| CN1310963C (en) | Catalyst component for olefin polymerization reaction and catalyst | |
| CN1771266B (en) | Magnesium dichloride-alcohol adducts and catalyst components obtained therefrom | |
| CN1241954C (en) | Catalyst component for alkene polyreaction and its catalyst | |
| CN1176258A (en) | Catalyst system to produce highly crystalline polypropylene | |
| CN1310964C (en) | Catalyst component for olefin polymerization reaction and catalyst | |
| CN1752115A (en) | Catalyst used for ethylene polymerization or copolymerization and its preparation method | |
| CN100429242C (en) | Catalyst components for olefinic polyreaction and catalyst thereof | |
| CN1257920C (en) | Catalyst component for olefinic polymerization and its catalyst | |
| CN1310967C (en) | Catalyst component for olefin polymerization reaction and its catalyst | |
| CN1743347A (en) | Catalyst component for olefinic polymerization and its catalyst | |
| CN1178961C (en) | Solid catalyst component for olefine polymerizing reaction and catalyst with the component |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20070418 |