CN103012627A - Olefin polymerization catalyst ingredient, preparation method and use of the olefin polymerization catalyst ingredient, catalyst system, use of the catalyst system, and olefin polymerization method - Google Patents
Olefin polymerization catalyst ingredient, preparation method and use of the olefin polymerization catalyst ingredient, catalyst system, use of the catalyst system, and olefin polymerization method Download PDFInfo
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Abstract
The invention relates to a preparation method of an olefin polymerization catalyst ingredient. The preparation method comprises the following steps that 1, a uniform solution of a magnesium halide-alcohol adduct is prepared; 2, the uniform solution obtained by the step 1 and a titanium compound undergo a contact reaction in the presence of separation assistants to produce a mixture; and 3, the mixture obtained by the step 2 and an internal donor compound undergo a contact reaction to produce a suspension liquid, wherein the separation assistants comprise a separation assistant A, a separation assistant B and a separation assistant C; the separation assistant A is a glycol ester compound shown in the formula (I); the separation assistant B is an alkyl ester of an aliphatic or aromatic carboxylic acid; the separation assistant C is a titanate compound; and the separation assistant A is different from the separation assistant B. The invention also relates to the olefin polymerization catalyst ingredient, a use of the olefin polymerization catalyst ingredient, a catalyst system, a use of the catalyst system, and an olefin polymerization method. Catalyst particles prepared from the olefin polymerization catalyst ingredient have good particle morphology and have a high polymerization activity and good dynamic performances in propylene polymerization.
Description
Technical field
The present invention relates to a kind of preparation method of the catalyst component for olefinic polymerization, the catalyst component that is used for olefinic polymerization by the method preparation, described catalyst component for olefinic polymerization is in the application of the catalyst system that is used for olefinic polymerization, a kind of catalyst system for olefinic polymerization, the catalyst body that should be used for olefinic polymerization ties up to application and the olefine polymerizing process of olefinic polyreaction.
Background technology
With magnesium, titanium, halogen and the electron donor solid particulate type polyolefin catalyst as basal component, be first magnesium chloride to be prepared into homogeneous solution, pass through again the active ingredient of crystallization and load titaniferous.Separate out in the system in dissolving, only have the existence of precipitation additive, just might obtain even-grained solids, precipitation additive generally adopts the compounds such as organic acid anhydride, organic acid, ketone, ether, ester.
The titanium-containing catalyst component is to be dissolved in organic epoxy compounds and organo phosphorous compounds forms homogeneous solution by magnesium halide in CN85100997A, and this solution mixes with the titanium tetrahalide or derivatives thereof, in the presence of precipitation additive such as organic acid anhydrides, separates out solids; This solids is processed with the multi-carboxylate, and it is attached on the solids, processes with titanium tetrahalide and inert diluent and obtains.When this catalyzer was used for propylene polymerization, catalyst activity was higher, and the degree of isotacticity of resulting polymers is higher, and apparent density is large.But preparation technology's more complicated of this catalyzer, raw materials used of a great variety, reaction process is longer.Simultaneously, the productive rate of this method Kaolinite Preparation of Catalyst and catalyst performance all remain further to be improved.
CN1042156A also discloses and has a kind ofly adopted eutectoid to go out the standby catalyst system of legal system, the Ti ingredient of solid catalyst that contains in this catalyst system is in the decane solvent, the solid magnesium dichloride is dissolved in organic alcohol compound such as the 2-Ethylhexyl Alcohol, after adding the organic acid anhydride dissolving, under the titanium tetrahalide effect, separate out precipitation, obtain main catalyst component through processing such as titanium tetrahalides again.This catalyzer is used for propylene polymerization, and catalyst activity is higher, and morphology is better.But this catalyzer used titanium tetrachloride amount in building-up process is larger, and the polymkeric substance degree of isotacticity is lower slightly, and the productive rate of catalyzer and catalyst performance all remain further to be improved.
CN1436766A discloses a kind of polyol ester compounds, and this compound is suitable for the preparation of the catalyzer of olefinic polymerization.All described the polyolefin catalyst active ingredient that obtains as internal electron donor take this special polynary ester compound among CN1436796A, the CN1453298A, this catalyzer has higher activity and stereospecificity preferably.But during the method Kaolinite Preparation of Catalyst, because polyol ester is to be carried on catalyst surface after granules of catalyst forms, load may not be even, simultaneously, in order to obtain preferably catalyst performance, the usage quantity of binary alcohol esters is larger, and the data that this point is given from patent also embody to some extent.
CN1763108A discloses a kind of catalyst component for olefinic polymerization and preparation method, containing the Ti ingredient of solid catalyst is in solvent oil, the solid magnesium dichloride is dissolved in organic alcohol compound such as the 2-Ethylhexyl Alcohol, after adding the dissolving of organic acid anhydride and titanic acid ester, under the titanium tetrahalide effect, separate out precipitation, obtain main catalyst component through processing such as titanium tetrahalides again.This catalyzer is used for propylene polymerization, and morphology is better.But this catalyzer used titanium tetrachloride amount in building-up process is larger, and catalyst activity is lower slightly, and the productive rate of catalyzer and polymerization all remain further to be improved.
Summary of the invention
First purpose of the present invention is the low defective of catalytic activity when overcoming catalyst component that the catalyst component preparation method that adopts existing olefinic polymerization prepares and being used for the catalyst system polymerization, and a kind of preparation method of the new catalyst component that is used for olefinic polymerization is provided.
Second purpose of the present invention provides the catalyst component that is used for olefinic polymerization that adopts above-mentioned preparation method's preparation.
The 3rd purpose of the present invention provides described catalyst component for olefinic polymerization in the application of the catalyst system that is used for olefinic polymerization.
The 4th purpose of the present invention provides a kind of catalyst system for olefinic polymerization.
The 5th purpose of the present invention provides the application that described catalyst body for olefinic polymerization ties up to olefinic polyreaction.
The 6th purpose of the present invention provides a kind of olefine polymerizing process.
The invention provides a kind of preparation method of catalyst component of olefinic polymerization, the method may further comprise the steps:
(1) magnesium halide and alcohol compound are carried out the first contact reacts in the presence of hydrocarbon solvent, form homogeneous solution;
(2) in the presence of precipitation additive, step (1) gained homogeneous solution and titanium compound are carried out the second contact reacts to separate out solid precipitation, obtain containing the mixture of solid precipitation;
(3) mixture and the internal electron donor compound with step (2) gained carries out the 3rd contact reacts, obtains suspension;
Wherein, described precipitation additive comprises precipitation additive a, precipitation additive b and precipitation additive c, and described precipitation additive a is the diol ester compound shown in the formula (I),
In the formula (I), R
1-R
2Identical or different, be respectively separately and replace or the C of unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
R
3-R
8Identical or different, be respectively separately the C of hydrogen, halogen, replacement or unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
Perhaps R
3-R
6In at least one and R
7-R
8In at least one Cheng Huan;
Described precipitation additive b is the alkyl ester of aliphatics or aromatic carboxylic acid;
Described precipitation additive c is that general formula is Ti (OR
9)
nX
4-nThe titanate ester compound, R
9For carbonatoms is that alkyl or the carbonatoms of 1-10 is the 3-10 cycloalkyl, X is halogen; 1≤n≤4, n is integer, and,
Described precipitation additive a is different from described precipitation additive b.
The present invention also provides the catalyst component that is used for olefinic polymerization by the aforesaid method preparation.
The present invention also provides the application of described catalyst component for olefinic polymerization at the catalyst system that is used for olefinic polymerization.
The present invention also provides a kind of catalyst system for olefinic polymerization, and this catalyzer contains: (1) described catalyst component for olefinic polymerization provided by the invention; (2) alkylaluminium cpd; And (3) optional external donor compound.
The present invention also provides described catalyst body for olefinic polymerization to tie up to the application of olefinic polyreaction.
The present invention also provides a kind of olefine polymerizing process, and the method comprises: under the olefinic polymerization condition, one or more alkene are contacted with catalyst system provided by the invention, at least a in the described alkene is by general formula CH
2The alkene that=CHR represents, wherein R is that hydrogen or carbonatoms are the alkyl of 1-6.
The present invention compares with prior art, because catalyst component of the present invention uses polyol ester compound, alkyl-carboxylic acid ester compound, the composite precipitation additive of titanate ester compound by special construction to replace in the prior art with Tetra hydro Phthalic anhydride and titanic acid ester as precipitation additive in preparation process, make the catalyst component for preparing when having preferably particle form, yield with greater catalytic agent, the catalyst component that obtains show high polymerization activity and good dynamic performance when being used for olefinic polymerization.
Embodiment
According to the preparation method of described catalyst component for olefinic polymerization provided by the invention, the method can may further comprise the steps:
(1) magnesium halide and alcohol compound are carried out the first contact reacts in the presence of hydrocarbon solvent, form homogeneous solution;
(2) in the presence of precipitation additive, step (1) gained homogeneous solution and titanium compound are carried out the second contact reacts to separate out solid precipitation, obtain containing the mixture of solid precipitation;
(3) mixture and the internal electron donor compound with step (2) gained carries out the 3rd contact reacts, obtains suspension;
Wherein, described precipitation additive comprises precipitation additive a, precipitation additive b and precipitation additive c, and described precipitation additive a is the diol ester compound shown in the formula (I),
In the formula (I), R
1-R
2Identical or different, be respectively separately and replace or the C of unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
R
3-R
8Identical or different, be respectively separately the C of hydrogen, halogen, replacement or unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
Perhaps R
3-R
6In at least one and R
7-R
8In at least one Cheng Huan;
Described precipitation additive b is the alkyl ester of aliphatics or aromatic carboxylic acid;
Described precipitation additive c is that general formula is Ti (OR
9)
nX
4-nThe titanate ester compound, R
9For carbonatoms is that alkyl or the carbonatoms of 1-10 is the 3-10 cycloalkyl, X is halogen; 1≤n≤4, n is integer, and,
Described precipitation additive a is different from described precipitation additive b.
According to the present invention, step (1) is to step (3), and the consumption of described alcohol compound, titanium compound, internal electron donor compound and magnesium halide can carry out appropriate selection according to the composition of the catalyst component that is used for olefinic polymerization of expecting.For example, the mol ratio of described alcohol compound, titanium compound, internal electron donor compound and described magnesium halide can be 2-4: 5-35: 0.01-3: 1; Be preferably 2.5-3.5: 8-25: 0.02-0.3: 1, described titanium compound is in titanium elements, and described adduct of magnesium halides is in magnesium elements.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, in step (1), the described first catalytic purpose is in order to make magnesium halide, alcohol compound form the adducts homogeneous solution of magnesium halide and alcohol in the presence of varsol.The present invention does not have concrete restriction to carrying out the first contact reacts with the condition that forms homogeneous solution, can determine according to the concrete halogenated magnesium compound that uses.Under the preferable case, the first contact reacts of formation homogeneous solution can be closed under the condition at alcohol and be carried out, and the described alcohol condition of closing can comprise that usually temperature is 30-150 ℃, is preferably 60-140 ℃; Time is 0.5-10 hour, is preferably 0.5-6 hour.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, in the step (1), can be as 1 take the mol ratio of the magnesium halide of magnesium elements and alcohol compound: 2-4 be preferably 1: 2.5-3.5.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, one or more of the derivative that described magnesium halide can be replaced by alkyl or halogen-oxyl for the complex compound of the water of magnesium dihalide, magnesium dihalide or alcohol, one or two halogen atom in the magnesium dihalide molecular formula.Among the present invention, what described halogen can be in fluorine, chlorine, bromine and the iodine is at least a, is preferably chlorine and/or bromine.The concrete example of magnesium halide can be in magnesium dichloride, dibrominated magnesium, chlorination phenoxy group magnesium, chlorination isopropoxy magnesium, the chlorination butoxy one or more, is preferably anhydrous magnesium dichloride.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, described alcohol compound can be in Fatty Alcohol(C12-C14 and C12-C18), alicyclic ring alcohol and the aromatic alcohol one or more.Wherein to be preferably straight chain or carbonatoms that carbonatoms is 1-10 be the branched fatty alcohol of 3-10 to Fatty Alcohol(C12-C14 and C12-C18); Alicyclic ring alcohol is preferably the alicyclic ring alcohol that carbonatoms is 3-12; Aromatic alcohol is preferably the alkylaryl alcohol that aryl alcohol that carbonatoms is 6-20 or carbonatoms are 7-20.The concrete example of alcohol compound can be in ethanol, propyl alcohol, butanols, 2-Ethylhexyl Alcohol, phenylcarbinol, the phenylethyl alcohol one or more, is preferably 2-Ethylhexyl Alcohol.
Preparation method according to the catalyst component of olefinic polymerization of the present invention, in the preparation process of the catalyst component of described olefinic polymerization, chemically interactive varsol can variously not occur with magnesium halide alcohol adduct as what this area was commonly used in the varsol that uses in the step (1), concrete example can be one or more of alkane, naphthenic hydrocarbon, aromatic hydrocarbon, be preferably in decane, the benzene,toluene,xylene one or more, more preferably toluene.
Preparation method according to the catalyst component of olefinic polymerization of the present invention, in the step (2) in the presence of precipitation additive, step (1) gained homogeneous solution and titanium compound are carried out the second contact reacts to separate out solid precipitation, the mixture that obtains containing solid precipitation is not particularly limited, can carry out with reference to prior art, for example the titanium compound in the step (2) can be separately and the homogeneous solution of step (1) gained in the presence of precipitation additive, react, after also titanium compound can being mixed with inert diluent and the homogeneous solution of step (1) gained in the presence of precipitation additive, react.Under the preferable case, the homogeneous solution that titanium compound is mixed rear and step (1) gained with inert diluent reacts in the presence of precipitation additive.Usually, according to the preparation method of the catalyst component for olefinic polymerization of the present invention, what the inert diluent that mixes with titanium compound can be in hexane, heptane, octane, decane, benzene, toluene and the dimethylbenzene is at least a.The mol ratio of magnesium and inert diluent can be 1: 9-27, preferred 1: 12-22.According to the present invention, the described second catalytic condition in the step (2) comprises: in the presence of precipitation additive, step (1) gained homogeneous solution and titanium compound under-40 ℃ to 0 ℃ temperature, are contacted 3-5 hour, then be warming up to 50-150 ℃; Preferably, in the presence of precipitation additive, step (1) gained homogeneous solution is contacted 3.5-4.5 hour with titanium compound under-30 ℃ to-20 ℃ temperature, then be warming up to 90-130 ℃.In the step (2), can be under-40 ℃ to 0 ℃ temperature, the homogeneous solution that first titanium compound and step (1) is obtained mixes, and then adds precipitation additive solution contact 3-5 hour, then is warming up to 50-150 ℃, obtains containing the mixture of solid precipitation; Perhaps first precipitation additive solution is joined in the homogeneous solution that step (1) obtains, then under-40 ℃ to 0 ℃ temperature, be warming up to 50-150 ℃ contact 3-5 hour with titanium compound after, obtain containing the mixture of solid precipitation; Preferably first precipitation additive solution is joined in the homogeneous solution that step (1) obtains, then under-40 ℃ to 0 ℃ temperature, be warming up to 50-150 ℃ contact 3-5 hour with titanium compound after, obtain containing the mixture of solid precipitation; More preferably first precipitation additive solution is joined in the homogeneous solution that step (1) obtains, then under-30 ℃ to-20 ℃ temperature, be warming up to 90-130 ℃ contact 3.5-4.5 hour with titanium compound after, obtain containing the mixture of solid precipitation.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, respectively in magnesium elements with in titanium elements, the mol ratio of magnesium halide and titanium compound can be 1 in the step (2): 5-35, preferred 1: 8-25; The mol ratio of magnesium halide and precipitation additive is 1: 0.025-0.9 is preferably 1: 0.05-0.33, more preferably 1: 0.1-0.23.
Usually, according to the catalyst component for olefinic polymerization of the present invention, wherein the titanium compound in titanium compound described in the step (2) and the aftermentioned step (4) can be identical or different, can be separately the conventional various titanium compounds that use in this area, can be Ti (OR for three halogenated titaniums and/or general formula separately for example
10)
mX
4-mShown titanium compound, in this general formula, R
10Can be alkyl, be preferably C
1-C
10Alkyl, X can be halogen, such as Cl, Br or I, 0≤m≤3, m is integer.Preferably, described titanium compound is one or more in titanium tetrachloride, titanium tetrabromide, titanium tetra iodide, alkoxyl group three halogenated titaniums, dialkoxy dihalide titanium, the tri-alkoxy halogenated titanium, is preferably titanium tetrachloride.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, wherein, in step (2), with respect to 1 mole the magnesium halide in magnesium elements, described precipitation additive a add-on can be the 0.005-0.1 mole, is preferably the 0.01-0.05 mole; Described precipitation additive b add-on can be the 0.01-0.5 mole, is preferably the 0.02-0.2 mole; The add-on of described precipitation additive c can be the 0.01-0.3 mole, is preferably the 0.02-0.08 mole.
Usually, according to the needs of practical application, particularly for the catalyst component that is used for propylene polymerization, in order to obtain the propene polymer of high isotactic, in the preparation process of described catalyst component, also need to add at least a internal electron donor compound.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, the 3rd catalytic condition comprises in the step (3), and temperature of reaction is 20-120 ℃, is preferably 70-110 ℃; Reaction times is 0.5-6 hour, is preferably 1-4 hour.In the magnesium halide of magnesium elements, the mol ratio of magnesium halide and internal electron donor compound can be 1: 0.01-3 is preferably 1: 0.02-0.3.
Preparation method according to the catalyst component for olefinic polymerization of the present invention, described internal electron donor compound can be this area various internal electron donor compounds commonly used, for example, described internal electron donor compound can be the binary alcohol esters compounds shown in the formula (I), aliphatics except formula (I) or aromatic monocarboxylate's alkyl ester, the alkyl ester of aliphatics or aromatic polycarboxylic acid, fatty ether, in cycloaliphatic ether and the aliphatic ketone one or more, be preferably the aliphatic carboxylic acid esters, of binary, in aromatic carboxylic acid esters and the diether compound one or more, more preferably phthalate, the malonic ester class, succinate compound, the glutarate class, in pivalate or the carbonates one or more.Concrete example can be diethyl phthalate, diisobutyl phthalate, n-butyl phthalate, dimixo-octyl phthalate, dinoctyl phthalate, diethyl malonate, butyl ethyl malonate, 2,3-di-isopropyl ethyl succinate, 2,3-di-isopropyl di-iso-octyl succinate, 2,3-di-isopropyl dibutyl succinate, 2,3-di-isopropyl succsinic acid dimethyl esters, 2,2-dimethyl succinate diisobutyl ester, 2-Ethyl-2-Methyl di-iso-octyl succinate, 2-Ethyl-2-Methyl ethyl succinate, diethylene adipate, Polycizer W 260, ethyl sebacate, Uniflex DBS, diethyl maleate, maleic acid n-butyl, the naphthalene dicarboxylic acids diethyl ester, the naphthalene dicarboxylic acids dibutylester, triethyl trimellitate, tributyl trimellitate, biphenyl three triethylenetetraminehexaacetic acid esters, connection benzenetricarboxylic acid tri-n-butyl, the pyromellitic acid tetra-ethyl ester, in pyromellitic acid four butyl esters one or more most preferably are diisobutyl phthalate and/or n-butyl phthalate.
Of particular note, among the present invention, described internal electron donor compound can be the material partly or entirely identical with described precipitation additive, when described internal electron donor compound partly or entirely identical with described precipitation additive, can be when adding precipitation additive, replace partly or completely internal electron donor with precipitation additive, but the granules of catalyst form for preparing in this case is relatively poor.Also can be when adding internal electron donor, replace part or all of precipitation additive with internal electron donor, but the catalyzer for preparing in this case is only high in polyreaction catalytic activity in early stage, and the catalytic activity of polymerization reaction late stage is low, and the catalytic activity cycle of the catalyzer of gained is short.Therefore, even if described internal electron donor compound is partly or entirely identical with described precipitation additive, also preferably in step (2) and step (3), add respectively according to the method described in the present invention.
Preparation method according to the catalyst component of olefinic polymerization of the present invention, wherein, described precipitation additive a can be 2-ethyl-1, the ammediol dibenzoate, 2-propyl group-1, the ammediol dibenzoate, 2-sec.-propyl-2-isopentyl-1,3 propylene glycol dibenzoates, 1,3-butyleneglycol mesitylenic acid ester, the 2-methyl isophthalic acid, 3-butyleneglycol two m-chlorobenzoic acid esters, 2,3-dimethyl-1,3-butyleneglycol dibenzoate, 1,3-pentanediol pivalate, 2,4-pentanediol dibenzoate, the 2-methyl isophthalic acid, 3-pentanediol phenylformic acid laurate, 2,2-dimethyl-1,3-pentanediol dibenzoate, 2,4-heptanediol dibenzoate, 2-methyl-3, at least a in the 5-heptanediol dibenzoate etc., preferred 3,5-heptanediol dibenzoate, 4-ethyl-3,5-heptanediol dibenzoate, at least a in 2, the 4-pentanediol dibenzoate.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, wherein, the carbonatoms of the aliphatic carboxylic acid among the described precipitation additive b is preferably 1-8; The carbonatoms of aromatic carboxylic acid is preferably 7-10; The carbonatoms of alkyl is preferably 1-10.Described precipitation additive b can be in benzoic acid alkyl base ester, bialkyl ortho phthalate, the hexanedioic acid dialkyl ester at least a, be preferably at least a in ethyl benzoate, diethyl phthalate, n-butyl phthalate, diisobutyl phthalate, dimixo-octyl phthalate, dinoctyl phthalate, diethylene adipate, the Polycizer W 260, more preferably n-butyl phthalate and/or diisobutyl phthalate.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, wherein, the R among the described precipitation additive c
9Carbonatoms be preferably 2-6; Further preferred described precipitation additive c is one or more in tetrabutyl titanate, tetraethyl titanate and the isopropyl titanate, is preferably tetrabutyl titanate.
According to the preparation method of the catalyst component of olefinic polymerization of the present invention, wherein, under the preferable case, the method is further comprising the steps of:
(4) solid-liquid suspension that step (3) is obtained separates, and solid ingredient and the titanium compound that solid-liquid separation obtains carried out the 4th contact reacts.
In the step (4), the titanium compound of described titanium compound and abovementioned steps (2) is identical or different, does not repeat them here.
When method of the present invention comprises step (4), can make the concentration in the titanium active centre that is carried on the magnesium halide surface higher, thereby further improve catalytic activity.
The titanium compound type of service is not particularly limited in the step (4), for example the titanium compound in the step (4) can be separately reacts with solid product after the solid-liquid suspension of step (3) gained separates, also titanium compound and inert diluent can be mixed with solid product after the solid-liquid suspension of step (3) gained separates and react.The kind of described inert diluent is described in detail at preamble, does not repeat them here.The 4th contact reacts condition in the step (4) comprises temperature of reaction 50-150 ℃, is preferably 80-120 ℃; Reaction times 1-6 hour, be preferably 2.5-4.5 hour.After reaction finishes, filter out the liquid in the reactant, obtain solid reaction product, then repeat the 4th contact reacts 1-3 time, through washing, drying obtains the solid catalytic ingredient of titaniferous.In the step (4), the mol ratio of magnesium halide and titanium compound can be 1: 3-40, preferred 1: 5-35.
A preferred embodiment of the invention, the method for the catalyst component of preparation olefinic polymerization provided by the invention can be carried out in accordance with the following steps:
(1) under varsol, with Magnesium Chloride Anhydrous and 0.5-10 hour (being preferably 0.5-6 hour) of alcohol compound 30-150 ℃ (being preferably 60-140 ℃) reaction, obtain uniform alcohol adduct solution, wherein, the mol ratio of Magnesium Chloride Anhydrous and alcohol compound is 1: 2-4 (is preferably 1: 2.5-3.5);
(2) with the diol-lipid compound a, the mixed solution of the ester compound b of aliphatics or aromatic carboxylic acid and the composite formation of titanate ester compound c is as precipitation additive, precipitation additive is joined in the above-mentioned alcohol adduct solution, the mol ratio of Magnesium Chloride Anhydrous and diol-lipid compound a is 1: 0.005-0.1 (is preferably 1: 0.01-0.05), the mol ratio of Magnesium Chloride Anhydrous and ester compound b is 1: (be preferably 1: 0.02-0.2), the mol ratio of Magnesium Chloride Anhydrous and titanate ester compound c is 1: 0.01-0.3 (is preferably 1: 0.02-0.08) to 0.01-0.5;
(3) with the above-mentioned alcohol adduct solution that is added with precipitation additive, join in the mixture of-40 ℃ to 0 ℃ titanium compound and inert diluent, make them in-40 ℃ to 0 ℃ (being preferably-30 ℃ to-20 ℃) lower fully contact by stirring, after 3-5 hour (being preferably 3.5-4.5 hour), be warming up to 50-150 ℃ (being preferably 90-130 ℃), separate out solid precipitation in the temperature-rise period, wherein, the mol ratio of Magnesium Chloride Anhydrous and titanium compound is 1: 5-35 (is preferably 1: 8-25);
(4) in the mixture that step (3) obtains, add ester compound as internal electron donor, temperature be 20-120 ℃ (being preferably 70-110 ℃) reaction 0.5-6 hour (being preferably 1-4 hour), obtain suspended substance, wherein, the mol ratio of Magnesium Chloride Anhydrous and ester compound is 1: 0.01-3 (is preferably 1: 0.02-0.3);
(5) reactant that step (4) is obtained, filter out liquid, the mixture that adds again titanium compound and inert diluent, under 50-150 ℃, (be preferably 80-120 ℃), continue 1-6 hour (being preferably 2.5-4.5 hour) of reaction, reaction filters out liquid after finishing, and obtains solid product.Repeat with the reaction of the mixture of solid product and titanium compound and inert diluent 1-3 time, through washing, drying.The mol ratio of Magnesium Chloride Anhydrous and titanium compound is 1: 3-40 (is preferably 1: 5-35).
The present invention also provides the catalyst component of prepared according to the methods of the invention olefinic polymerization.
The present invention also provides the catalyst according to the invention component to be suitable for preparing olefin polymerization catalyst system.
According to olefin polymerization catalyst system of the present invention, this catalyst system is used for by general formula CH
2The polyreaction of the alkene that=CHR represents, wherein R is that hydrogen or carbonatoms are the alkyl of 1-6, described catalyst system comprises the reaction product of following material:
(1) catalyst component of above-mentioned olefinic polymerization;
(2) alkylaluminium cpd;
(3) randomly, external donor compound.
In above-mentioned olefin polymerization catalysis, described alkylaluminium cpd can be the field of olefin polymerisation various alkylaluminium cpds that can be used as the promotor of Ziegler-natta catalyst commonly used.In the preferred case, described alkylaluminium cpd can be the compound shown in the formula (II),
AlR′
n′X′
3-n′ (II)
In the formula (II), R ' is that hydrogen, carbonatoms are that alkyl or the carbonatoms of 1-20 is the aryl of 6-20, and X ' is halogen, and n ' is the integer of 1-3.The object lesson of described alkylaluminium cpd for example can be in trimethyl aluminium, triethyl aluminum, triisobutyl aluminium, trioctylaluminum, a hydrogen diethyl aluminum, a hydrogen diisobutyl aluminum, aluminium diethyl monochloride, a chloro-di-isobutyl aluminum, sesquialter ethyl aluminum chloride and the ethyl aluminum dichloride at least a.
Among the present invention, the consumption of described alkylaluminium cpd can be the conventional amount used of this area.Usually, the mol ratio of the aluminium in the described alkylaluminium cpd and the titanium in the described catalyzer is 5-5000: 1.Preferably, the mol ratio of the aluminium in the described alkylaluminium cpd and the titanium in the described catalyzer is 20-1000: 1.More preferably, the mol ratio of the aluminium in the described alkylaluminium cpd and the titanium in the described catalyzer is 50-500: 1.
Because only the precipitation additive in the olefin polymerization catalyst components preparation process is improved in olefin polymerization catalysis of the present invention, therefore, kind and the content of the external donor compound in the olefin polymerization catalysis of the present invention are not particularly limited.In the preferred case, the aluminium in the described alkylaluminium cpd and the mol ratio of described external donor compound are 0.1-500: 1, and preferred 1-300: 1, more preferably 3-100: 1.
In above-mentioned olefin polymerization catalysis, described external electron donor component can be the silicoorganic compound shown in the formula (III),
R″
m′Si(OR″′)
4-m′ (III)
In the formula (III), R " a kind of in the haloalkyl that is 1-20 for halogen, hydrogen atom, carbonatoms are the alkyl of 1-20, cycloalkyl that carbonatoms is 3-20, carbonatoms is 6-20 aryl and carbonatoms; R ' " a kind of in the haloalkyl that is 1-20 for carbonatoms is the alkyl of 1-20, cycloalkyl that carbonatoms is 3-20, carbonatoms is 6-20 aryl and carbonatoms; M ' is the integer of 1-3.Specific examples as described silicoorganic compound can be the trimethylammonium methoxy silane, trimethylethoxysilane, trimethyl phenoxysilane, dimethyldimethoxysil,ne, dimethyldiethoxysilane, methyl-t-butyldimethoxysilane, dimethoxydiphenylsilane, the phenylbenzene diethoxy silane, Dicyclohexyldimethoxysilane, diisopropyl dimethoxy silane, phenyltrimethoxysila,e, phenyl triethoxysilane, vinyltrimethoxy silane, Cyclohexyl Methyl Dimethoxysilane, dicyclopentyl dimethoxyl silane, 2-ethyl piperidine base-2-tertiary butyl dimethoxy silane, (1,1,1-three fluoro-2-propyl group)-2-ethyl piperidine base dimethoxy silane and (1,1,1-three fluoro-2-propyl group)-and at least a in the methyl dimethoxysilane etc., be preferably Cyclohexyl Methyl Dimethoxysilane, diisopropyl dimethoxy silane, at least a in the dimethoxydiphenylsilane.
The catalyst according to the invention system is applicable in the olefinic polyreaction.
According to olefine polymerizing process of the present invention, the method is included under the olefinic polymerization condition, and one or more alkene are contacted with above-mentioned catalyst system, and at least a in the described alkene is by general formula CH
2The alkene that=CHR represents, wherein R is that hydrogen or carbonatoms are the alkyl of 1-6.
Olefine polymerizing process of the present invention can be used for the equal polymerization of alkene, also can be used for multiple alkene is carried out copolymerization.At least a in the described alkene is by general formula CH
2The alkene that=CHR represents, wherein R is that hydrogen or carbonatoms are the alkyl of 1-6.Described by general formula CH
2The specific examples of the alkene that=CHR represents comprises: ethene, propylene, 1-n-butene, the positive amylene of 1-, 1-n-hexylene, the positive octene of 1-and 4-methyl-1-pentene.Preferably, described alpha-olefin CH
2=CHR is one or more in ethene, propylene, 1-butylene, 4-methyl-1-pentene and the 1-hexene.More preferably, described by general formula CH
2The alkene that=CHR represents is propylene.
According to olefine polymerizing process of the present invention, described olefinic polymerization condition can be the normal condition of this area.The consumption of catalyzer can be the consumption of the various catalyzer of prior art.
Describe the present invention in detail below in conjunction with embodiment, but be not used for limiting the present invention.
In following examples, the testing method that relates to is as follows:
1, the yield of catalyzer: the yield %=gained catalyst quality of catalyzer/used magnesium chloride quality * 100%
2, the titanium content in the catalyzer: test according to 721 spectrophotometers
3, catalyst grain size distributes: measure according to Ma Erwen 2000 normal hexane dispersion agent laser diffractometries.
4, the mensuration of melt index (MI): measure according to GB/T3682-2000.
5, propene polymer isotacticity index (II) adopts the heptane extraction process to measure: the dry polymer samples of 2 grams, be placed in the extractor with the extracting of boiling heptane after 6 hours, the polymer weight (g) that residuum is dried to the constant weight gained is degree of isotacticity with the ratio of 2 (g).
6, the butene polymers degree of isotacticity adopts the ether extraction method to measure, and measures under the 2.16kg load.
7, molecular weight distribution MWD (MWD=Mw/Mn): employing PL-GPC220 is the (standard specimen: polystyrene, flow velocity: 1.0ml/min, pillar: 3xPlgel10um MlxED-B 300x7.5nm) of the mensuration under 150 ℃ take trichlorobenzene as solvent.
Embodiment 1-3 is used for illustrating olefin polymerization catalyst components of the present invention, olefin polymerization catalysis and olefine polymerizing process.
Embodiment 1
(1) preparation of catalyst component
In the reactor that repeats to replace through High Purity Nitrogen, add successively 52.5mmol (5.0g) Magnesium Chloride Anhydrous, 328mmol (35ml) toluene, 140mmol (22ml) 2-Ethylhexyl Alcohol, be under 110 ℃ the condition in mixing speed 450rpm, temperature, reacted 3.0 hours, and obtained the alcohol adduct solution of stable and uniform; Add again 3,5-heptanediol dibenzoate 0.8mmol (0.4ml), diisobutyl phthalate 5.6mmol (1.5ml), tetrabutyl titanate 2.2mmol (0.75ml) stirred 60 minutes, was cooled to room temperature.
Be added with 3 with above-mentioned, 5-heptanediol dibenzoate 0.8mmol (0.4ml), diisobutyl phthalate 5.6mmol, the alcohol adduct homogeneous solution of tetrabutyl titanate 2.2mmol (0.75ml) joins through nitrogen fully replaces, be equipped with in the reactor of-20 ℃ 1.0mol (110ml) titanium tetrachloride and 190mmol (20ml) toluene, make them-20 ℃ of lower fully contacts by stirring, after 5 hours, be warming up to 110 ℃, separate out solid precipitation in the temperature-rise period, add dibutyl phthalate 5.6mmol (1.5ml), reacted 1 hour, after reaction finishes, filter out liquid, and then solid contacted 1 hour with 680mmol (72ml) toluene and 437mmol (48ml) titanium tetrachloride under 110 ℃, repeat again after the filtration with 680mmol (72ml) toluene and 437mmol (48ml) titanium tetrachloride 110 ℃ of lower and these solid contact reactss once.The solids that obtains is washed 5 times with 919mmol (120ml) hexane, then dry, obtain olefin polymerization catalyst components.
The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.
(2) polyacrylic preparation
A. polyacrylic preparation-1
In 5 liters of autoclaves, after gas-phase propene is fully replaced, at room temperature add the hexane solution (concentration of triethyl aluminum is 0.5 mmole/milliliter) of 5 milliliters of triethyl aluminums, the hexane solution (concentration of CHMMS is 0.1 mmole/milliliter) of l milliliter Cyclohexyl Methyl Dimethoxysilane (CHMMS), 10 milliliters of anhydrous hexanes and 10 milligrams of ingredients of solid catalyst.Close autoclave, introduce the hydrogen of 1.0NL and the liquid propene of 1.15Kg; Under stirring state, temperature is risen to 70 ℃ in 10 minutes.70 ℃ of polyreactions 60 minutes stop stirring after reaction finishes, and remove unpolymerized propylene monomer, and collected polymer is at 70 ℃ of lower vacuum-dryings 1 hour, the calculating catalyst activity of weighing.
The catalyst body that contains catalyst component ties up to polymerization activity in the propylene polymerization and the performance perameter of polymkeric substance is shown in Table 2.
B. polyacrylic preparation-2
Except polymerization temperature changes 95 ℃ into, all the other are with polyacrylic preparation-1.
The catalyst body that contains catalyst component ties up to polymerization activity in the propylene polymerization and the performance perameter of polymkeric substance is shown in Table 2.
(3) preparation of polybutene
In 5 liters of autoclaves, after the gas phase 1-butylene is fully replaced, at room temperature add the hexane solution (concentration of triethyl aluminum is 0.5 mmole/milliliter) of 5 milliliters of triethyl aluminums, the hexane solution (concentration of DIPMS is 0.1 mmole/milliliter) of l milliliter diisopropyl dimethoxy silane (DIPMS), 10 milliliters of anhydrous hexanes and 20 milligrams of ingredients of solid catalyst.Close autoclave, introduce the hydrogen of 1.0NL and the liquid 1-butylene of 1.0kg; Under stirring state, temperature is risen to 60 ℃ in 10 minutes.60 ℃ of polyreactions 2 hours stop stirring after reaction finishes, and remove unpolymerized 1-butylene monomer, and collected polymer is at 60 ℃ of lower vacuum-dryings 1 hour, the calculating catalyst activity of weighing.
The catalyst body that contains catalyst component ties up to polymerization activity in the butene polymerization and the performance perameter of butene polymers is shown in Table 3.
Embodiment 2
To add 3 among the embodiment 1,5-heptanediol dibenzoate 0.8mmol (0.4ml), diisobutyl phthalate 5.6mmol (1.5ml), tetrabutyl titanate 2.2mmol (0.75ml) changes into and adds 4-ethyl-3,5-heptanediol dibenzoate 2.6mmol, n-butyl phthalate 10.5mmol, isopropyl titanate 4.4mmol, all the other are with embodiment 1.
The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.
The catalyst body of catalyst component preparation ties up to polymerization activity in the propylene polymerization and the performance perameter of propene polymer is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of butene polymers is shown in Table 3.
Embodiment 3
To add 3 among the embodiment 1,5-heptanediol dibenzoate 0.8mmol (0.4ml), diisobutyl phthalate 5.6mmol (1.5ml), tetrabutyl titanate 2.2mmol (0.75ml), change into and add 2,4-pentanediol dibenzoate 1.3mmol (0.4g), diisobutyl phthalate 1.05mmol, tetraethyl titanate 1.05m mol, all the other are with embodiment 1.
The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.
The catalyst body of catalyst component preparation ties up to polymerization activity in the propylene polymerization and the performance perameter of propene polymer is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of butene polymers is shown in Table 3.
Comparative example 1
Except Kaolinite Preparation of Catalyst component in accordance with the following methods, all the other are with embodiment 1.
(1) preparation of catalyst component
In the reactor that repeats to replace through High Purity Nitrogen, add successively 52.5mmol (5.0g) Magnesium Chloride Anhydrous, 206mmol (40ml) decane, 152mmol (24ml) 2-Ethylhexyl Alcohol, be under 130 ℃ the condition in mixing speed 450rpm, temperature, reacted 2.0 hours, then add 2.2mmol (0.75ml) tetrabutyl titanate and 6.8mmol (1.0g) Tetra hydro Phthalic anhydride, continue reaction 1 hour, be cooled to room temperature, obtain the alcohol adduct solution of stable and uniform.
The alcohol adduct homogeneous solution of the above-mentioned 2.2mmol of being added with (0.75ml) tetrabutyl titanate and 6.8mmol (1.0g) Tetra hydro Phthalic anhydride is added to through nitrogen fully replaces, be equipped with in-20 ℃ the reactor of 1821mmol (200ml) titanium tetrachloride, make them-20 ℃ of lower fully contacts by stirring, after 4 hours, be warming up to 110 ℃, add diisobutyl phthalate 12.7mmol (3.4ml), reacted 2 hours, after reaction finishes, filter out liquid, add again 1821mmol (200ml) titanium tetrachloride, under 110 ℃, continue reaction 2 hours, after reaction finishes, filter out liquid, with 919mmol (120ml) hexane washing 5 times, drying makes the solid titanium catalyst component.
The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.
Carry out the preparation of propene polymer and butene polymers according to the method for embodiment 1.The performance perameter that the catalyst body of catalyst component preparation ties up to the polymerization activity in the propylene polymerization and prepares propene polymer is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of butene polymers is shown in Table 3.
Comparative example 2
Add 3,5-heptanediol dibenzoate 0.8mmol (0.4ml) with adding diisobutyl phthalate 12.7 (3.4ml) in the comparative example 1, changing into, diisobutyl phthalate 11.2mmol (3.0ml), all the other are with comparative example 1.The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.The catalyst body of catalyst component preparation ties up to polymerization activity in the propylene polymerization and the performance perameter of polymkeric substance is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of polymkeric substance is shown in Table 3.
Comparative example 3
Among the embodiment 1, alcohol adduct solution with do not add tetrabutyl titanate before TiCl4 contacts.The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.The catalyst body of catalyst component preparation ties up to polymerization activity in the propylene polymerization and the performance perameter of propene polymer is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of butene polymers is shown in Table 3.
Comparative example 4
Among the embodiment 1, alcohol adduct solution and TiCl
4Do not add diisobutyl phthalate before the contact.The result of the content of the titanium content of catalyst component, precipitation additive a and the size-grade distribution of catalyst component is as shown in table 1.The catalyst body of catalyst component preparation ties up to polymerization activity in the propylene polymerization and the performance perameter of polymkeric substance is shown in Table 2.The catalyst body of catalyst component preparation ties up to polymerization activity in the butene polymerization and the performance perameter of polymkeric substance is shown in Table 3.
Comparative example 5
Among the embodiment 1, alcohol adduct solution and TiCl
4Do not add 3,5-heptanediol dibenzoate before the contact, this scheme catalyst-free is separated out.
Table 1 catalyst component result contrast
Table 2 propylene polymerization performance comparison
Table 31-butene polymerization performance comparison
Can find out that from table 1, table 2, table 3 data the prepared catalyzer of the present invention all has good performance at aspects such as composition, particle form, polymerizations.Embodiment 1 is compared and can find out with comparative example 3,4,5, adopt compound precipitation additive of the present invention, adopt precipitation additive a+ precipitation additive b, precipitation additive a+ precipitation additive c, precipitation additive b+ precipitation additive c can proof load the magnesium chloride of titanium compound separate out, and the catalyst component for preparing is all to have good polymerization activity, the especially active height when the propylene high-temperature polymerization when propylene polymerization or butene polymerization.Embodiment 1 is compared and can find out with comparative example 1, adopt compound precipitation additive of the present invention, when being precipitation additive Kaolinite Preparation of Catalyst component than available technology adopting Tetra hydro Phthalic anhydride and titanic acid ester, the active height of the catalyzer for preparing, especially when the propylene high-temperature polymerization, the catalytic activity of the catalyst system for preparing of the present invention is apparently higher than the polymerization activity of the catalyzer for preparing of comparative example 1, and the polymkeric substance that polymerization obtains also shows higher degree of isotacticity and melting index.Embodiment 1 is compared and can find out with comparative example 2, the alkyl ester that before titanium compound is carried on magnesium chloride, adds diol-lipid compound and aromatic carboxylic acid, than the alkyl ester that adds again diol-lipid compound and aromatic carboxylic acid after titanium compound is carried on magnesium chloride, the activity cycle that obtains catalyst component of preparation is long, catalytic activity is especially high when the propylene high-temperature polymerization.
Claims (16)
1. the preparation method of the catalyst component of an olefinic polymerization, the method may further comprise the steps:
(1) magnesium halide and alcohol compound are carried out the first contact reacts in the presence of hydrocarbon solvent, form homogeneous solution;
(2) in the presence of precipitation additive, step (1) gained homogeneous solution and titanium compound are carried out the second contact reacts to separate out solid precipitation, obtain containing the mixture of solid precipitation;
(3) mixture and the internal electron donor compound with step (2) gained carries out the 3rd contact reacts, obtains suspension;
Wherein, described precipitation additive comprises precipitation additive a, precipitation additive b and precipitation additive c, and described precipitation additive a is the diol ester compound shown in the formula (I),
In the formula (I), R
1-R
2Identical or different, be respectively separately and replace or the C of unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
R
3-R
8Identical or different, be respectively separately the C of hydrogen, halogen, replacement or unsubstituted straight chain
1-C
20Alkyl, replacement or unsubstituted side chain C
3-C
20Alkyl, replacement or unsubstituted C
3-C
20Cycloalkyl, replacement or unsubstituted C
6-C
20Aryl, replacement or unsubstituted C
7-C
20Alkaryl, replacement or unsubstituted C
7-C
20Aralkyl, replacement or unsubstituted C
2-C
10Alkylene or replacement or unsubstituted C
10-C
20Fused ring aryl;
Perhaps R
3-R
6In at least one and R
7-R
8In at least one Cheng Huan;
Described precipitation additive b is the alkyl ester of aliphatics or aromatic carboxylic acid;
Described precipitation additive c is that general formula is Ti (OR
9)
nX
4-nThe titanate ester compound, R
9For carbonatoms is that alkyl or the carbonatoms of 1-10 is the 3-10 cycloalkyl, X is halogen; 1≤n≤4, n is integer, and,
Described precipitation additive a is different from described precipitation additive b.
2. method according to claim 1, wherein, the mol ratio of described alcohol compound, titanium compound, internal electron donor compound and described magnesium halide is 2-4: 5-35: 0.01-3: 1; Be preferably 2.5-3.5: 8-25: 0.02-0.3: 1, described titanium compound is in titanium elements, and described magnesium halide is in magnesium elements.
3. method according to claim 1, wherein, in step (2), with respect to 1 mole the magnesium halide in magnesium elements, the add-on of described precipitation additive a is the 0.005-0.1 mole, is preferably the 0.01-0.05 mole; The add-on of described precipitation additive b is the 0.01-0.5 mole, is preferably the 0.02-0.2 mole; The add-on of described precipitation additive c is the 0.01-0.3 mole, is preferably the 0.02-0.08 mole.
4. the described method of any one according to claim 1-3, wherein, described precipitation additive a is 2-ethyl-1, the ammediol dibenzoate, 2-propyl group-1, the ammediol dibenzoate, 2-sec.-propyl-2-isopentyl-1,3 propylene glycol dibenzoates, 1,3-butyleneglycol mesitylenic acid ester, the 2-methyl isophthalic acid, 3-butyleneglycol two m-chlorobenzoic acid esters, 2,3-dimethyl-1,3 butylene glycol dibenzoate, 1,3-pentanediol pivalate, 2,4-pentanediol dibenzoate, the 2-methyl isophthalic acid, 3-pentanediol phenylformic acid laurate, 2,2-dimethyl-1,3-pentanediol dibenzoate, 2,4-heptanediol dibenzoate and 2-methyl-3, at least a in the 5-heptanediol dibenzoate is preferably 3,5-heptanediol dibenzoate, 4-ethyl-3, at least a in 5-heptanediol dibenzoate and 2, the 4 pentanediol dibenzoates.
5. the described method of any one according to claim 1-4, wherein, the carbonatoms of the aliphatic carboxylic acid among the described precipitation additive b is 1-8; The carbonatoms of aromatic carboxylic acid is 7-10; The carbonatoms of alkyl is 1-10.
6. method according to claim 5, wherein, described precipitation additive b is at least a in ethyl benzoate, diethyl phthalate, n-butyl phthalate, diisobutyl phthalate, dimixo-octyl phthalate, dinoctyl phthalate, diethylene adipate and the Polycizer W 260, is preferably n-butyl phthalate and/or diisobutyl phthalate.
7. the described method of any one according to claim 1-6, wherein, the R among the described precipitation additive c
9Carbonatoms be 2-6; Described precipitation additive c is preferably one or more in tetrabutyl titanate, tetraethyl titanate and the isopropyl titanate.
8. the described method of any one according to claim 1-7, wherein, the method is further comprising the steps of:
(4) solid-liquid suspension that step (3) is obtained separates, and solid ingredient and the titanium compound that solid-liquid separation obtains carried out the 4th contact reacts.
9. method according to claim 8, wherein, described alcohol compound is one or more in Fatty Alcohol(C12-C14 and C12-C18), alicyclic ring alcohol and the aromatic alcohol; Described hydrocarbon solvent is one or more in straight or branched alkane, naphthenic hydrocarbon and the aromatic hydrocarbon; Described internal electron donor compound is one or more in the binary alcohol esters compounds shown in the formula (I), the aliphatics except formula (I) or aromatic monocarboxylate's alkyl ester, fatty ether, cycloaliphatic ether and the aliphatic ketone of alkyl ester, aliphatics or aromatic polycarboxylic acid; Described titanium compound is that general formula is Ti (OR
10)
mX
4-mCompound, wherein: R
10Be alkyl; X is halogen; 0≤m≤3, m is integer.
10. the catalyst component of the olefinic polymerization that the described method of any one prepares among the claim 1-9.
11. the application of catalyst component claimed in claim 10 in the preparation olefin polymerization catalyst system.
12. a catalyst system that is used for olefinic polymerization, this catalyst system contains:
(1) catalyst component for olefinic polymerization claimed in claim 10;
(2) alkylaluminium cpd; And
(3) optional external donor compound.
13. catalyst system according to claim 12, wherein, in the described alkylaluminium cpd of aluminium with take the mol ratio of the described catalyst component of titanium as 5-5000: 1, be preferably 20-1000: 1; Take the mol ratio of the described alkylaluminium cpd of aluminium and described external donor compound as 0.1-500: 1, preferred 1-300: 1, more preferably 3-100: 1.
14. according to claim 12 or 13 described catalyst systems, wherein, described alkylaluminium cpd is the compound shown in the formula (II),
AlR′
n′X′
3-n′ (II)
In the formula (II), R ' is that hydrogen, carbonatoms are that alkyl or the carbonatoms of 1-20 is the aryl of 6-20, and X ' is halogen, and n ' is the integer of 1-3; Described external donor compound is the silicoorganic compound shown in the formula (III),
R″
m′Si(OR″′)
4-m′ (III)
In the formula (III), R " a kind of in the haloalkyl that is 1-20 for halogen, hydrogen atom, carbonatoms are the alkyl of 1-20, cycloalkyl that carbonatoms is 3-20, carbonatoms is 6-20 aryl and carbonatoms; R ' " a kind of in the haloalkyl that is 1-20 for carbonatoms is the alkyl of 1-20, cycloalkyl that carbonatoms is 3-20, carbonatoms is 6-20 aryl and carbonatoms; M ' is the integer of 1-3.
15. the described catalyst body of any one ties up to the application in the olefinic polyreaction among the claim 12-14.
16. an olefine polymerizing process, the method is included under the olefinic polymerization condition, and one or more alkene are contacted with the described catalyst system of any one among the claim 12-14, and at least a in the described alkene is by general formula CH
2The alkene that=CHR represents, wherein R is that hydrogen or carbonatoms are the alkyl of 1-6.
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| CN106608937A (en) * | 2015-10-27 | 2017-05-03 | 中国石油化工股份有限公司 | Catalyst component for olefin polymerization, preparation method and application thereof |
| CN106608937B (en) * | 2015-10-27 | 2019-04-19 | 中国石油化工股份有限公司 | Catalytic component and its preparation method and application for olefinic polymerization |
| EP3798241A4 (en) * | 2018-05-21 | 2022-06-22 | China Petroleum & Chemical Corporation | Catalyst component for olefin polymerization, preparation method thereof, and catalyst including same |
| US20210205787A1 (en) * | 2018-05-21 | 2021-07-08 | China Petroleum & Chemical Corporation | Catalyst component for olefin polymerization, preparation method thereof, and catalyst including same |
| WO2019223683A1 (en) | 2018-05-21 | 2019-11-28 | 中国石油化工股份有限公司 | Catalyst component for olefin polymerization, preparation method thereof, and catalyst including same |
| US12121880B2 (en) * | 2018-05-21 | 2024-10-22 | China Petroleum & Chemical Corporation | Catalyst component for olefin polymerization, preparation method thereof, and catalyst including same |
| CN114456288A (en) * | 2020-10-22 | 2022-05-10 | 中国石油化工股份有限公司 | Titanium-containing catalyst, catalyst for olefin polymerization reaction, and preparation method and application thereof |
| CN114456289A (en) * | 2020-10-22 | 2022-05-10 | 中国石油化工股份有限公司 | Titanium-containing catalyst, catalyst for olefin polymerization, and preparation method and application thereof |
| CN114456288B (en) * | 2020-10-22 | 2024-02-13 | 中国石油化工股份有限公司 | Titanium-containing catalyst, catalyst for olefin polymerization reaction, preparation method and application thereof |
| CN114456289B (en) * | 2020-10-22 | 2024-02-13 | 中国石油化工股份有限公司 | Titanium-containing catalyst, catalyst for olefin polymerization, preparation method and application thereof |
| CN116041574A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Catalyst component for olefin polymerization and application thereof |
| CN116041576A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Olefin polymerization catalyst precursor, olefin polymerization catalyst carrier, preparation method and application thereof |
| CN116041578A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Catalyst component, preparation method thereof, catalyst system and application thereof |
| CN116041582A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Olefin polymerization catalyst solid component, preparation method thereof, catalyst system and application thereof |
| CN116041574B (en) * | 2021-10-28 | 2024-08-20 | 中国石油化工股份有限公司 | Catalyst component for olefin polymerization and application thereof |
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| CN103012627B (en) | 2015-03-11 |
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