CN109280103A - A kind of catalyst system and its application for olefinic polymerization - Google Patents
A kind of catalyst system and its application for olefinic polymerization Download PDFInfo
- Publication number
- CN109280103A CN109280103A CN201710591181.3A CN201710591181A CN109280103A CN 109280103 A CN109280103 A CN 109280103A CN 201710591181 A CN201710591181 A CN 201710591181A CN 109280103 A CN109280103 A CN 109280103A
- Authority
- CN
- China
- Prior art keywords
- compound
- och
- catalyst system
- catalyst
- alkyl
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
Abstract
The invention belongs to olefin polymerization catalysis field, a kind of catalyst system for olefinic polymerization and its application are specifically disclosed.The catalyst system includes the reaction product of following components: 1) ingredient of solid catalyst includes the reaction product of following components: alkoxyl magnesium compound, titanium compound and optional internal electron donor compound；2) co-catalyst: it is selected from organo-aluminum compound；3) at least one of three black false hellebore hydrocarbons and their derivates of ring shown in formula (I), M in formula (I) external donor compound: are selected from1、M2、M3、M4、M5And M6It is identical or different, it each is selected from hydrogen, hydroxyl, amino, aldehyde radical, carboxyl, acyl group, halogen atom ,-R1Or-OR2, wherein R1And R2Respectively substituted or unsubstituted C1~C10Alkyl, substituent group are selected from hydroxyl, amino, aldehyde radical, carboxyl, acyl group, halogen atom, alkoxy or hetero atom.
Description
Technical field
The invention belongs to olefin polymerization catalysis fields, and in particular to a kind of catalyst system for olefinic polymerization and its
Using.
Background technique
In the past 60 years, with the continuous development of olefin polymerization catalysis technology, Ziegler-Natta type polyolefin catalyst
Activity, hydrogen tune susceptibility and copolymerization performance and the bulk density of its polymer powder material, melt index, molecular weight distribution, fine powder
The parameters such as content and copolymerization units distribution have obtained significant optimization.But it is to be able to better adapt to industrial need
It asks, produces the superior product of performance, then the above-mentioned parameter of such catalyst and its polymerization powder also needs to further increase.
In the prior art, its hydrogen tune susceptibility can be improved by introducing internal electron donor into catalyst, such as:
CN1958620A introduces type siloxane electron donor；CN1743347A introduces benzoic ether/carboxylic of ortho alkoxy substitution
Acid esters (or diether) compounds electron donor；CN102295717A and CN103772536A introduces benzoate compounds conduct
Electron donor, to improve the hydrogen response of catalyst.Can also by into catalyst introduce inside/outside electron donor,
To improve the copolymerization performance of catalyst, such as: CN1726230A introduces ether, ester, amine, ketone or nitrile electronic donor compound；
CN1798774A is using alcohol, glycol, ester, ketone, amine, amide, nitrile, alkoxy silane and fatty ether as electron donor compound；
CN101050248A introduces alcohol, ketone, amine, amide, nitrile, alkoxy silane, fatty ether and aliphatic carboxylic acid esters' electron donor.
It records according to prior art, in the polymerization process of Ziegler-Natta type polypropylene catalyst, introduces outer give
Electron is the well-known technique in the field with the property for adjusting polymer；However, in Ziegler-Natta type polyethylene catalysts
Polymerization process introduce external electron donor report it is then less.Studies have shown that such as in Ziegler-Natta type polyethylene catalysts
Polymerization process introduce external electron donor, then the parameters such as the activity of catalyst, hydrogen tune susceptibility and copolymerization performance can not all must
To optimization, partial properties reduce instead.Ziegler-Natta type polyethylene catalysts external electron donor skill due to the above reasons,
Art not yet industrializes, and report in the prior art is less.
Therefore, it is urgent to provide a kind of external electron donors, can improve Ziegler-Natta type polyolefin catalyst simultaneously
The parameters such as activity, hydrogen tune susceptibility and copolymerization performance.
Summary of the invention
In order to solve the above-mentioned problems in the prior art, the present invention provides a kind of caltalyst for olefinic polymerization
System and its application, by introducing the external electron donor-ring with special nature in Ziegler-Natta type polyolefin catalyst
Three black false hellebore hydrocarbons and their derivates can improve activity, hydrogen tune susceptibility and the copolymerization performance of catalyst simultaneously.
According to the first aspect of the invention, the present invention provides a kind of catalyst system for olefinic polymerization, the catalysis
Agent system includes the reaction product of following components:
1) ingredient of solid catalyst:
Reaction product comprising following components: alkoxyl magnesium compound, titanium compound and optional internal electron donor chemical combination
Object；
2) co-catalyst:
Selected from organo-aluminum compound, the general formula of the organo-aluminum compound is AlR1 dX1 3-d, R in formula1For hydrogen or Cl~C20
Alkyl, X1For halogen atom, 0 d≤3 <；
3) external donor compound:
At least one of three black false hellebore hydrocarbons and their derivates of ring shown in formula (I),
M in formula (I)1、M2、M3、M4、M5And M6It is identical or different, it each is selected from hydrogen, hydroxyl, amino, aldehyde radical, carboxyl, acyl
Base, halogen atom ,-R1Or-OR2, wherein R1And R2Respectively substituted or unsubstituted C1~C10Alkyl, substituent group be selected from hydroxyl,
Amino, aldehyde radical, carboxyl, acyl group, halogen atom, alkoxy or hetero atom；
As two group M adjacent on phenyl ring1And M2Or M3And M4Or M5And M6It each is selected from-R1Or-OR2When, two
It is optionally mutually cyclic between a adjacent group.
According to the second aspect of the invention, the present invention provides a kind of above-mentioned caltalysts to tie up in olefin polymerization
Using.
Catalyst system for olefinic polymerization of the invention is used as by using three black false hellebore hydrocarbons and their derivates of ring and gives outside
Electron, can improve activity, hydrogen response and the copolymerization performance of catalyst simultaneously, in addition, using catalyst of the invention
The bulk density and copolymerization units content for the polymerization powder that system is prepared increase.
Specific embodiment
To keep the present invention easier to understand, below in conjunction with specific embodiment, the present invention will be described in detail, these realities
It applies mode and only serves illustrative, be not intended to restrict the invention.
According to the first aspect of the invention, the present invention provides a kind of catalyst system for olefinic polymerization, the catalysis
Agent system includes the reaction product of following components:
1) ingredient of solid catalyst:
Reaction product comprising following components: alkoxyl magnesium compound, titanium compound and optional internal electron donor chemical combination
Object；
2) co-catalyst:
Selected from organo-aluminum compound, the general formula of the organo-aluminum compound is AlR1 dX1 3-d, R in formula1For hydrogen or Cl~C20
Alkyl, X1For halogen atom, 0 d≤3 <；
3) external donor compound:
At least one of three black false hellebore hydrocarbons and their derivates of ring shown in formula (I),
M in formula (I)1、M2、M3、M4、M5And M6It is identical or different, it each is selected from hydrogen, hydroxyl, amino, aldehyde radical, carboxyl, acyl
Base, halogen atom ,-R1Or-OR2, wherein R1And R2Respectively substituted or unsubstituted C1~C10Alkyl, substituent group be selected from hydroxyl,
Amino, aldehyde radical, carboxyl, acyl group, halogen atom, alkoxy or hetero atom；
As two group M adjacent on phenyl ring1And M2Or M3And M4Or M5And M6It each is selected from-R1Or-OR2When, two
It is optionally mutually cyclic between a adjacent group.
In the present invention, alkyl can be alkyl, naphthenic base, alkenyl, alkynyl, aryl or aralkyl.Wherein, C1~C10Alkyl
Refer to C1~C10Straight chained alkyl or C3~C10Branched alkyl, non-limiting example includes: methyl, ethyl, n-propyl, different
Propyl, normal-butyl, sec-butyl, isobutyl group, tert-butyl, n-pentyl, isopentyl, tertiary pentyl, neopentyl, n-hexyl, n-heptyl, just
Octyl, dimethylhexanyl and positive decyl.
C3~C10The example of naphthenic base can include but is not limited to: cyclopropyl, cyclopenta, cyclohexyl, 4- methylcyclohexyl,
4- ethylcyclohexyl, 4- n-propyl cyclohexyl and 4- normal-butyl cyclohexyl.
C6~C10The example of aryl can include but is not limited to: phenyl, 4- aminomethyl phenyl and 4- ethylphenyl.
C2~C10The example of alkenyl can include but is not limited to: vinyl and allyl.
C2~C10The example of alkynyl can include but is not limited to: acetenyl and propargyl.
C7~C10The example of aralkyl can include but is not limited to: phenyl methyl, phenylethyl, phenyl n-propyl, phenyl
Normal-butyl, phenyl t-butyl and propyloxy phenyl base.
In the present invention, " substituted C1~C10Alkyl " refer to " C1~C10Alkyl " on a hydrogen atom (preferably hydrogen
Atom) or carbon atom replaced by the substituent group.
The hetero atom refers to the three black false hellebore hydrocarbons and their derivates of other rings other than halogen atom, carbon atom and hydrogen atom
Molecular structure on the atom that generally comprises, such as O, N, S, P, Si and B etc..
According to the present invention, the interior Donor compound can be selected from internal electron donor a and/or internal electron donor b.
Wherein, the internal electron donor a is selected from least one of three black false hellebore hydrocarbons and their derivates of ring shown in formula (I)；
The internal electron donor a and the external donor compound can be identical or different.
The internal electron donor b can be other interior electrons commonly used in the art different from internal electron donor a
Body, can selected from Organic Alcohol, organic acid, organic acid esters, organic acid halides, organic acid anhydride, ether, ketone, amine, phosphate, amide,
Carbonic ester, phenol, pyridine and high-molecular compound with polar group etc..
Specifically, the internal electron donor b can be selected from methyl acetate, ethyl acetate, propyl acetate, butyl acetate, acetic acid
N-octyl, methyl benzoate, ethyl benzoate, butyl benzoate, hexyl-benzoate, ethyl p-methyl benzoate, naphthoic acid first
Ester, naphthoic acid ethyl ester, methyl methacrylate, ethyl acrylate, butyl acrylate, ether, butyl ether, tetrahydrofuran, 2,2- bis-
Methyl-1,3- di ethyl propyl ether, methanol, ethyl alcohol, propyl alcohol, isopropanol, butanol, isooctanol, octylame, triethylamine, acetone, fourth
Ketone, cyclopentanone, 2- methyl-cyclopentanone, cyclohexanone, phenol, hydroquinone, ethylene oxide, propylene oxide, epoxychloropropane, phosphoric acid
Trimethyl, triethyl phosphate, tricresyl phosphate propyl ester, tributyl phosphate, triphenyl phosphate, tri hexyl phosphate, poly-methyl methacrylate
At least one of ester, polystyrene, Hydrin and polyethylene oxide.
Preferably, in formula (I), M1、M2、M3、M4、M5And M6It is identical or different, it is former each to be selected from hydroxyl, amino, aldehyde radical, halogen
Son ,-R1Or-OR2, and R1And R2It each is selected from by the substituted or unsubstituted C of halogen atom1~C10Alkyl.
It is highly preferred that the three black false hellebore hydrocarbons and their derivates of ring are selected from least one of following compound:
Compound A:M1=M2=M3=M4=M5=M6=OCH3；
Compound B:M1=M2=M3=M4=M5=M6=OCH2CH3；
Compound C:M1=M2=M3=M4=M5=M6=OCH2CH2CH3；
Compound D:M1=M2=M3=M4=M5=M6=OCH (CH3)2；
Compound E:M1=M2=M3=M4=M5=M6=OCH2CH2CH2CH3；
Compound F:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH3；
Compound G:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH3；
Compound H:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH2CH3；
Compound I:M1=M2=M3=M4=M5=M6=OH；
Compound J:M1=M3=M5=OCH3；M2=M4=M6=OH；
Compound K: M1=M3=M5=OCH3；M2=M4=M6=NH2；
Compound L: M1=M3=M5=OCH3；M2=M4=M6=Cl；
Compound M:M1=M3=M5=OCH3；M2=M4=M6=Br；
Compound N: M1=M3=M5=OCH3；M2=M4=M6=I；
Compound O:M1=M3=M5=OCH3；M2=M4=M6=CHO；
Compound P:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH2Br；
Compound Q: M1=M2=M3=M4=M5=M6=OCH2CH2Cl。
In addition, working as M1=M3=M5=X, M2=M4=M6(X, Y respectively indicate the above-mentioned M of the present invention to=Y1、M3、M5And M2、M4、
M6Selectable group, and X is different from Y) when, there may be following isomers: M for the three black false hellebore hydrocarbons and their derivates of ring1=M4
=M5=X, M2=M3=M6=Y.However the isomers is also within the scope of the present invention.
In the present invention, the three black false hellebore hydrocarbons and their derivates of ring can be prepared one of as follows:
Method 1: in the presence of acidic materials and optional halogenated hydrocarbons, by phenyl ring analog derivative A shown in formula (II) with
Formaldehyde or derivatives thereof is reacted, to obtain the three black false hellebore hydrocarbons and their derivates of ring；
Method 2: in the presence of acidic materials, phenyl ring analog derivative B shown in catalysis type (III) carries out condensation reaction, thus
To the three black false hellebore hydrocarbons and their derivates of ring；
Method 3: in the presence of a lewis acid, in halogenated hydrocarbons, phenyl ring analog derivative A and formaldehyde shown in catalysis type (II)
Or derivatives thereof reacted, to obtain the three black false hellebore hydrocarbons and their derivates of ring；
Wherein, to M7、M8、M9、M10Definition and M1~M6It is identical, details are not described herein.
The acidic materials can be selected from hydrochloric acid, perchloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, pyrosulfuric acid, sulfurous acid, phosphorus
Acid, pyrophosphoric acid, at least one of phosphorous acid, boric acid, formic acid, acetic acid, benzoic acid, trifluoroacetic acid, sulfonic acid and benzene sulfonic acid.
The halogenated hydrocarbons can be selected from carbon tetrachloride, chloroform, methylene chloride, bromomethane, monochlorethane, a chlorine third
Alkane, a chlorobutane, a chloropentane, a chlorohexane, bromic ether, 1,2- dichloroethanes, 1,3- dichloropropane, bis- neoprene of 1,4-
In alkane, 1,5- dichloropentane, 1,6- dichloro hexane, chlorocyclopentane, chlorocyclohexane, monochloro-benzene, dichloro-benzenes and bromobenzene
It is at least one.
The lewis acid can be selected from least one in boron trifluoride ether, ferric trichloride, alchlor and titanium tetrachloride
Kind.
The derivative of formaldehyde can be selected from paraformaldehyde, for example, metaformaldehyde.
In the above each method, the dosage of various raw materials is referred to routine techniques selection, repeats no more herein.
According to the present invention, the general formula of the alkoxyl magnesium compound is represented by Mg (OR3)a(OR4)2-a, R3And R4Respectively
Substituted or unsubstituted C1~C10Alkyl, substituent group are hydroxyl, amino, aldehyde radical, carboxyl, acyl group, halogen atom, alkoxy or miscellaneous original
Son, 0≤a≤2.
Preferably, the alkoxyl magnesium compound is selected from Mg (OEt)a(OEHA)2-a, 1.5≤a≤2 or Mg (OEt)a
(OBu)2-a, 1.3≤a≤2；Wherein, Et is ethyl, EHA is 2- ethylhexyl, Bu is butyl.
The alkoxyl magnesium compound carrier is referred to preparation method in the prior art and obtains, and the present invention does not make this
It is particularly limited to.
According to the present invention, the titanium compound can be the conventional selection of this field, and general formula can be Ti (OR2)nX2 4-n, wherein R2For C1~C8Alkyl, preferably C1~C8Alkyl；X2For Cl, Br or I, 0≤n≤4.
Specifically, the titanium compound can be selected from TiCl4、TiBr4、TiI4、Ti(OC2H5)Cl3、Ti(OCH3)Cl3、Ti
(OC4H9)Cl3、Ti(OC2H5)Br3、Ti(OC2H5)2Cl2、Ti(OCH3)2Cl2、Ti(OCH3)2I2、Ti(OC2H5)3Cl、Ti
(OCH3)3Cl、Ti(OC2H5)3I、Ti(OC2H5)4、Ti(OC3H7)4With Ti (OC4H9)4At least one of.
Preferably, the titanium compound is selected from TiCl4、Ti(OC2H5)Cl3、Ti(OCH3)Cl3、Ti(OC4H9)Cl3And Ti
(OC4H9)4At least one of.It is highly preferred that the titanium compound is TiCl4。
According to the present invention, in the ingredient of solid catalyst, in terms of every mole of magnesium, the dosage of the titanium compound is 0.1
~15mol；The dosage of the internal electron donor compound is 0~0.1mol, preferably 0~0.08mol.
In the present invention, the ingredient of solid catalyst is by the way that the alkoxyl magnesium compound is first dispersed in atent solvent
In suspension is made, add other reactant compositions and carry out made from haptoreactions.
Preferably, the ingredient of solid catalyst can be prepared using following methods:
Method 1
1) alkoxyl magnesium compound is dispersed in atent solvent, obtains suspension；
2) by the suspension and titanium compound haptoreaction, unreacted reactant is then removed, and is washed with atent solvent；
3) sediment and the titanium compound and optional interior electron in the presence of an inert solvent, obtaining step 2)
Then body a haptoreaction removes unreacted reactant and solvent, washing precipitate, obtains the ingredient of solid catalyst.
Method 2
1) alkoxyl magnesium compound is dispersed in atent solvent, obtains suspension；
2) by the suspension and titanium compound and optional internal electron donor b haptoreaction, unreacted reactant is then removed,
And it is washed with atent solvent；
3) sediment and the titanium compound and optional interior electron in the presence of an inert solvent, obtaining step 2)
Then body a haptoreaction removes unreacted reactant and solvent, washing precipitate, obtains the ingredient of solid catalyst.
Method 1 can specifically include:
S1: the alkoxyl magnesium compound is dispersed in atent solvent, suspension is obtained；
S2: -20 to 20 DEG C at a temperature of, the titanium compound is added into the suspension；
S3: being warming up to 50-95 DEG C, reacts 0.5-5 hours under agitation, is then allowed to stand layering, extracts supernatant liquor,
Sediment is washed with atent solvent；
S4: being added titanium compound and optional internal electron donor a is stirred to react 0.5-5 hours at 50-95 DEG C, removes
Unreacted reactant and solvent are then allowed to stand layering, extract supernatant liquor, and sediment is washed with atent solvent, obtains the solid and urge
Agent component.
Method 2 can specifically include:
S1: the alkoxyl magnesium compound is dispersed in atent solvent, suspension is obtained；
S2: -20 to 20 DEG C at a temperature of, the titanium compound and optional interior electron are added into the suspension
Body b；
S3: being warming up to 50-95 DEG C, reacts 0.5-5 hours under agitation, is then allowed to stand layering, extracts supernatant liquor,
Sediment is washed with atent solvent；
S4: being added titanium compound and optional internal electron donor a is stirred to react 0.5-5 hours at 50-95 DEG C, removes
Unreacted reactant and solvent are then allowed to stand layering, extract supernatant liquor, and sediment is washed with atent solvent, obtains the solid and urge
Agent component.
The S2 in S4 and method 2 in method 1 can be carried out stage by stage, each stage be separately added into different reactive components into
Row reaction.
Selected atent solvent can be identical or different in above each step, and can refer to the prior art and selected,
This is not particularly limited in the present invention.For example, the atent solvent is toluene and/or hexane.
In addition, method made above is description of illustrating in more detail to ingredient of solid catalyst of the present invention, but the present invention
It is not limited to these preparation methods.
According to the present invention, the organo-aluminum compound can be selected from Al (CH3)3、Al(CH2CH3)3、Al(i-Bu)3、Al(n-
C6H13)3、AlH(CH2CH3)2、AlH(i-Bu)2、AlCl(CH2CH3)2、AlCl1.5(CH2CH3)1.5、AlCl(CH2CH3)2And AlCl2
(CH2CH3At least one of).
Preferably, the organo-aluminum compound is selected from Al (CH2CH3)3、Al(n-C6H13)3With Al (i-Bu)3In at least one
Kind.It is highly preferred that the organo-aluminum compound is Al (CH2CH3)3And/or Al (i-Bu)3。
According to the present invention, the molar ratio of the aluminium in the organo-aluminum compound and the titanium in the ingredient of solid catalyst can
Think 5 ︰, 1~500 ︰ 1,1~200 ︰ 1 of preferably 20 ︰.
According to the present invention, the molar ratio of the external donor compound and titanium in the ingredient of solid catalyst is 0.5 ︰
1~50 ︰ 1.
According to the second aspect of the invention, the present invention provides above-mentioned caltalysts to tie up to answering in olefin polymerization
With.
In the present invention, the olefin polymerization includes homopolymerization reaction and the copolymerization of alkene.
Specifically, catalyst system of the invention can be used for the homopolymerization of ethylene；It is ethylene and butylene, amylene, hexene, pungent
The combined polymerization of the combined polymerization of alkene or 4-methyl-1-pentene, preferably ethylene and butylene.
In addition, the catalyst system be suitable for it is various under the conditions of polymerization reaction, for example, the olefin polymerization can
To be carried out in liquid phase or gas phase, or can also be carried out under the operation that liquid phase is combined with gas phase polymerization stage.The temperature of polymerization
Degree can be 0~150 DEG C, preferably 60~90 DEG C.
Medium used by liquid phase polymerization can be selected from iso-butane, hexane, heptane, hexamethylene, naphtha, raffinate oil, add
The atent solvents such as the aliphatic saturated hydrocarbons such as hydrogen gasoline, kerosene, benzene,toluene,xylene or aromatic hydrocarbon, preferably toluene, n-hexane or
Hexamethylene.
In addition, making molecular weight regulator using hydrogen to adjust the molecular weight of final polymer.
The present invention will be described in detail by way of examples below.
In the following Examples and Comparative Examples:
1, in ingredient of solid catalyst titanium elements relative weight percents: use spectrophotometry.
2, the composition of ingredient of solid catalyst: liquid nuclear-magnetism is used1H-NMR。
3, it melt index (MI): according to ASTM D1238-99, load 2.16kg, measures at 190 DEG C.
4, copolymerization units content in polymer powders: liquid nuclear-magnetism is used13C-NMR is determined.
5, in polymer powders hexane extractable content weight percent: resulting whole powder slurries nitrogen will be polymerize
It is transferred in standard cylindrical container, is thoroughly dried in ventilation condition, obtain blocky powder, vertically cut the blocky powder of gained
20g is placed it in container after crushing, is extracted 2 hours at 50 DEG C with 300mL hexane, is then extracted 20mL extracting solution, set
In the surface plate being precisely weighed, the surface plate being completely dried is weighed, the mass weight gain of surface plate is m1G, and thus
The weight percent for calculating hexane extractable content is 75m1%.
6, in polymerization reaction, the pressure in kettle is absolute pressure.
Preparation example 1~4 is used to illustrate the preparation method of the three black false hellebore hydrocarbons and their derivates of ring.
Preparation example 1
Under condition of ice bath, 1,2- 1,2-dimethoxy benzene (1.0g) is added drop-wise to formalin (4mL/38%)/0.1mL tri-
It in the mixture of chloromethanes/concentrated hydrochloric acid (6mL), is reacted, after 30 minutes, solution becomes starchiness, continues stirring 4 at room temperature
Hour.Solid is collected by filtration, ice water washing thoroughly obtains 0.5g formula (IV) compound represented A after drying.
Preparation example 2
Under condition of ice bath, 3- methoxyl group -4- ethyoxyl-benzyl alcohol (3g) is dissolved in 30mL methanol, in ice bath and stirring
The perchloric acid 15mL of lower dropwise addition 65%.Under nitrogen protection, ice bath stirring 18h.30mL water is slowly added into reaction product, with
After make that organic phase is extracted with dichloromethane.After organic phase is carefully washed with sodium hydrate aqueous solution, then it is washed with deionized,
It is dry.It is purified after organic phase is thoroughly drained using column chromatography, obtains 1g such as formula (V) compound represented F.
Preparation example 3
1,2- neighbour's benzene diethyl ether (3.3g) and metaformaldehyde (0.63g) are dissolved in dry methylene chloride (30mL), ice
The lower stirring of bath, is slowly dropped into boron trifluoride ether (4.25g), after being added dropwise, removes ice-water bath, stirs 3h under room temperature, TLC with
Track reacts until the reaction is complete, stops reaction, and mixture is washed with water 3 times, separates organic layer, be spin-dried for organic solvent, obtain oil
Shape object is added a small amount of acetone and dissolves grease, then a large amount of methanol are added thereto, and being statically placed in refrigerator makes it that white be precipitated admittedly
Body.It filters, thoroughly after drying, obtains 1.5g formula (VI) compound represented B.
Preparation example 4
Under condition of ice bath, the bromo- benzyl alcohol of 3- methoxyl group -4- (3.6g) is dissolved in 30mL methanol, under ice bath and stirring
65% perchloric acid 15mL is added dropwise.Under nitrogen protection, ice bath stirring 18h.30mL water is slowly added into reaction product, then
Make that organic phase is extracted with dichloromethane.It after organic phase is carefully washed with sodium hydrate aqueous solution, then is washed with deionized, does
It is dry.It is purified after thoroughly draining using column chromatography, obtains 0.8g formula (VII) compound represented M.
Examples 1 to 3 is for illustrating that catalyst system and caltalyst of the invention tie up in olefin polymerization
Using.
Embodiment 1
(1) preparation of ingredient of solid catalyst
By 10g Mg (OEt)2, 55mL toluene be added in reaction kettle, formed under conditions of stirring rate 300rpm outstanding
Supernatant liquid.System is cooled to 0 DEG C, is slowly added to 30mL titanium tetrachloride, 90 DEG C are to slowly warm up to after being added dropwise to complete, constant temperature 1.5 is small
When.Stop stirring, stand, suspension is layered quickly, extracts supernatant liquor.60mL toluene and 30mL titanium tetrachloride are added, is risen
Temperature is to 90 DEG C, constant temperature 2 hours.Stop stirring, stand, extracts supernatant liquor.Through inert diluent toluene and organic solvent hexane
It is repeatedly dry after washing, the ingredient of solid catalyst a of good fluidity is obtained, composition is shown in Table 1.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added, 1.0mL concentration is 1M
Triethyl aluminum and 0.01mmol the compound A as made from preparation example 1, add by the above method prepare solid catalyst
Component a (titanium containing 0.6mg), is warming up to 70 DEG C, and being passed through hydrogen makes pressure in kettle reach 0.28MPa, then be passed through ethylene make in kettle it is total
Pressure reaches 0.73MPa, polymerize 2 hours under the conditions of 80 DEG C, polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added, 1.0mL concentration is 1M
Triethyl aluminum and 0.01mmol the compound A as made from preparation example 1, add by the above method prepare solid catalyst
Component a (titanium containing 0.6mg), is warming up to 70 DEG C, and being passed through hydrogen makes pressure in kettle reach 0.58MPa, then be passed through ethylene make in kettle it is total
Pressure reaches 0.73MPa, polymerize 2 hours under the conditions of 80 DEG C, polymerization result is shown in Table 2.
(3) copolymerization
Configure the gaseous mixture of ethylene/butylene first in distribution tank, the molar ratio of gaseous mixture be ethylene/butylene=
0.90/0.10。
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added, 1.0mL concentration is 1M
Triethyl aluminum and 0.01mmol the compound A as made from preparation example 1, add by the above method prepare solid catalyst
Component a (titanium containing 0.6mg), is warming up to 70 DEG C, and being passed through hydrogen makes pressure in kettle reach 0.28MPa, then is passed through ethylene/butylene mixing
Gas makes stagnation pressure in kettle reach 0.73MPa, polymerize 2 hours under the conditions of 80 DEG C, polymerization result is shown in Table 3.
Embodiment 2
(1) preparation of ingredient of solid catalyst
By 10g Mg (OEt)2, 55mL toluene be added in reaction kettle, formed under conditions of stirring rate 300rpm outstanding
Supernatant liquid.System is cooled to 0 DEG C, is slowly added to 40mL titanium tetrachloride, 90 DEG C, constant temperature 1 hour are to slowly warm up to after being added dropwise to complete.
Stop stirring, stand, suspension is layered quickly, extracts supernatant liquor.Add 60mL toluene, 30mL titanium tetrachloride and 0.2g by
Compound F made from preparation example 2 is warming up to 90 DEG C, constant temperature 1 hour.Stop stirring, stand, extracts supernatant liquor.It is dilute through inertia
Release agent toluene and organic solvent hexane repeatedly wash after it is dry, obtain the ingredient of solid catalyst b of good fluidity, composition is shown in Table 1.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.01mmol as made from preparation example 3
Compound B, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.01mmol as made from preparation example 3
Compound B, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 2.
(3) copolymerization
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.01mmol as made from preparation example 3
Compound B, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 3.
Embodiment 3
(1) preparation of ingredient of solid catalyst
By 10g Mg (OEt)1.7(OEHA)0.3, 60mL toluene be added in reaction kettle, in the condition of stirring rate 300rpm
Lower formation suspension.System is cooled to 0 DEG C, 60mL titanium tetrachloride and 0.5mL ethyl acetate is slowly successively added, is added dropwise to complete
After be to slowly warm up to 90 DEG C, constant temperature 2 hours.Stop stirring, stand, suspension is layered quickly, extracts supernatant liquor.It adds
60mL toluene and 50mL titanium tetrachloride are warming up to 90 DEG C, constant temperature 2 hours.Stop stirring, stand, extracts supernatant liquor.Through inertia
Diluent toluene and organic solvent hexane are dry after repeatedly washing, and obtain the ingredient of solid catalyst c of good fluidity, composition is shown in Table
1。
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.02mmol as made from preparation example 4
Compound M, and that add is ingredient of solid catalyst c, polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.02mmol as made from preparation example 4
Compound M, and that add is ingredient of solid catalyst c, polymerization result is shown in Table 2.
(3) copolymerization
With embodiment 1, but the type of external electron donor and additional amount are changed into 0.02mmol as made from preparation example 4
Compound M, and that add is ingredient of solid catalyst c, polymerization result is shown in Table 3.
Comparative example 1
(1) preparation of ingredient of solid catalyst
As described in Example 1.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added and 1.0mL concentration is 1M
Triethyl aluminum, add by the above method prepare ingredient of solid catalyst a (titanium containing 0.6mg), be warming up to 70 DEG C, be passed through
Hydrogen makes pressure in kettle reach 0.28MPa, then being passed through ethylene makes stagnation pressure in kettle reach 0.73MPa, and it is small that 2 are polymerize under the conditions of 80 DEG C
When, polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added and 1.0mL concentration is 1M
Triethyl aluminum, add by the above method prepare ingredient of solid catalyst a (titanium containing 0.6mg), be warming up to 70 DEG C, be passed through
Hydrogen makes pressure in kettle reach 0.58MPa, then being passed through ethylene makes stagnation pressure in kettle reach 0.73MPa, and it is small that 2 are polymerize under the conditions of 80 DEG C
When, polymerization result is shown in Table 2.
(3) copolymerization
Configure the gaseous mixture of ethylene/butylene first in distribution tank, the molar ratio of gaseous mixture be ethylene/butylene=
0.90/0.10。
Volume is the stainless steel cauldron of 2L, after high pure nitrogen is sufficiently displaced from, 1L hexane is added and 1.0mL concentration is 1M
Triethyl aluminum, add by the above method prepare ingredient of solid catalyst a (titanium containing 0.6mg), be warming up to 70 DEG C, be passed through
Hydrogen makes pressure in kettle reach 0.28MPa, then being passed through ethylene/butylene gaseous mixture makes stagnation pressure in kettle reach 0.73MPa, in 80 DEG C of items
It polymerize 2 hours under part, polymerization result is shown in Table 3.
Comparative example 2
(1) preparation of ingredient of solid catalyst
As described in Example 1.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With embodiment 1, but the type of external electron donor and additional amount are changed into the ethyl benzoate of 0.01mmol, gathers
Conjunction the results are shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With embodiment 1, but the type of external electron donor and additional amount are changed into the ethyl benzoate of 0.01mmol, gathers
Conjunction the results are shown in Table 2.
(3) copolymerization
With embodiment 1, but the type of external electron donor and additional amount are changed into the ethyl benzoate of 0.01mmol, gathers
Conjunction the results are shown in Table 3.
Comparative example 3
(1) preparation of ingredient of solid catalyst
As described in Example 2.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With comparative example 1, but that add is ingredient of solid catalyst b, and polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With comparative example 1, but that add is ingredient of solid catalyst b, and polymerization result is shown in Table 2.
(3) copolymerization
With comparative example 1, but that add is ingredient of solid catalyst b, and polymerization result is shown in Table 3.
Comparative example 4
(1) preparation of ingredient of solid catalyst
As described in Example 2.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With embodiment 1, but the type of external electron donor and additional amount are changed into 1, the 2- O-phthalic of 0.01mmol
Ether, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With embodiment 1, but the type of external electron donor and additional amount are changed into 1, the 2- O-phthalic of 0.01mmol
Ether, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 2.
(3) copolymerization
With embodiment 1, but the type of external electron donor and additional amount are changed into 1, the 2- O-phthalic of 0.01mmol
Ether, and that add is ingredient of solid catalyst b, polymerization result is shown in Table 3.
Comparative example 5
(1) preparation of ingredient of solid catalyst
As described in Example 3.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With comparative example 1, but that add is ingredient of solid catalyst c, and polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With comparative example 1, but that add is ingredient of solid catalyst c, and polymerization result is shown in Table 2.
(3) copolymerization
With comparative example 1, but that add is ingredient of solid catalyst c, and polymerization result is shown in Table 3.
Comparative example 6
(1) preparation of ingredient of solid catalyst
As described in Example 3.
(2) homopolymerization is reacted
1. low hydrogen gas/ethylene ratio polymerization reaction
With embodiment 1, but the type of external electron donor and additional amount are changed into the propyl acetate of 0.02mmol, and again
That be added is ingredient of solid catalyst c, and polymerization result is shown in Table 2.
2. the polymerization reaction of high hydrogen/ethylene ratio
With embodiment 1, but the type of external electron donor and additional amount are changed into the propyl acetate of 0.02mmol, and again
That be added is ingredient of solid catalyst c, and polymerization result is shown in Table 2.
(3) copolymerization
With embodiment 1, but the type of external electron donor and additional amount are changed into the propyl acetate of 0.02mmol, and again
That be added is ingredient of solid catalyst c, and polymerization result is shown in Table 3.
Table 1
*: not comprising the ethoxy group in three black false hellebore hydrocarbons and their derivates of ring.
Table 2
From the data of table 2:
1, invention catalyst system and is not added by addition three black false hellebore hydrocarbons and their derivates of ring as external electron donor
The catalyst system of external electron donor is compared, in low hydrogen second than can improve simultaneously poly- in the polymerization reaction with high hydrogen second ratio
The activity of catalyst for ethylene system, hydrogen tune susceptibility, and the bulk density of polymerization powder；
2, by other compounds (listed compound only serve it is illustrative, such as ethyl benzoate, propyl acetate and 1,2-
1,2-dimethoxy benzene) as external electron donor be added catalyst system after, the activity of catalyst system, hydrogen tune susceptibility, Yi Jiju
The bulk density for closing powder but decreases.
Table 3
| Number | External donor compound | Copolymerization units content (mol%) | Hexane extractable content (wt%) |
| Embodiment 1 | Compound A | 2.4 | 4.2 |
| Comparative example 1 | - | 2.2 | 5.3 |
| Comparative example 2 | Ethyl benzoate | 1.8 | 4.3 |
| Embodiment 2 | Compound B | 2.6 | 3.6 |
| Comparative example 3 | - | 2.5 | 3.9 |
| Comparative example 4 | 1,2- 1,2-dimethoxy benzene | 1.6 | 3.6 |
| Embodiment 3 | Compound M | 2.3 | 3.7 |
| Comparative example 5 | - | 2.1 | 5.2 |
| Comparative example 6 | Propyl acetate | 1.7 | 3.9 |
From the data of table 3:
1, after the present invention is by introducing catalyst system as external electron donor for three black false hellebore hydrocarbons and their derivates of ring, polymerization
The copolymerization units content of powder improves, and hexane extractable content is reduced.This explanation is with copolymerization units content in polymerization powder
It improves, the copolymerization units content in lower-molecular-weight component is reduced, and the copolymerization units content in medium/high molecular weight component improves.
It follows that three black false hellebore hydrocarbons and their derivates of ring improve the copolymerization performance of catalyst system, so that it is comprehensive to be conducive to product
The raising of energy.
2, by other compounds (listed compound only serve it is illustrative, such as ethyl benzoate, propyl acetate and 1,2-
1,2-dimethoxy benzene) introduce catalyst system as external electron donor after, copolymerization units content and the hexane for polymerizeing powder are extractable
Object reduces.This illustrates that above-mentioned external electron donor reduces the addition probability of comonomer, although hexane extractable content is also therewith
It reduces, but this is not the raising of catalyst system copolymerization performance.
The embodiment of the present invention is described above, above description is exemplary, and non-exclusive, and also not
It is limited to disclosed embodiment.Without departing from the scope and spirit of illustrated embodiment, for the art
Many modifications and changes are obvious for those of ordinary skill.
Claims (10)
1. a kind of catalyst system for olefinic polymerization, which is characterized in that the catalyst system includes the reaction of following components
Product:
1) ingredient of solid catalyst:
Reaction product comprising following components: alkoxyl magnesium compound, titanium compound and optional internal electron donor compound；
2) co-catalyst:
Selected from organo-aluminum compound, the general formula of the organo-aluminum compound is AlR1 dX1 3-d, R in formula1For hydrogen or Cl~C20Alkyl,
X1For halogen atom, 0 d≤3 <；
3) external donor compound:
At least one of three black false hellebore hydrocarbons and their derivates of ring shown in formula (I),
M in formula (I)1、M2、M3、M4、M5And M6It is identical or different, it each is selected from hydrogen, hydroxyl, amino, aldehyde radical, carboxyl, acyl group, halogen
Atom ,-R1Or-OR2, wherein R1And R2Respectively substituted or unsubstituted C1~C10Alkyl, substituent group be selected from hydroxyl, amino,
Aldehyde radical, carboxyl, acyl group, halogen atom, alkoxy or hetero atom；
As two group M adjacent on phenyl ring1And M2Or M3And M4Or M5And M6It each is selected from-R1Or-OR2When, two phases
It is optionally mutually cyclic between adjacent group.
2. catalyst system according to claim 1, wherein in formula (I), M1、M2、M3、M4、M5And M6It is identical or different,
It each is selected from hydroxyl, amino, aldehyde radical, halogen atom ,-R1Or-OR2, and R1And R2It each is selected from substituted or unsubstituted by halogen atom
C1~C10Alkyl.
3. catalyst system according to claim 1 or 2, wherein the three black false hellebore hydrocarbons and their derivates of ring are selected from following
At least one of compound:
Compound A:M1=M2=M3=M4=M5=M6=OCH3；
Compound B:M1=M2=M3=M4=M5=M6=OCH2CH3；
Compound C:M1=M2=M3=M4=M5=M6=OCH2CH2CH3；
Compound D:M1=M2=M3=M4=M5=M6=OCH (CH3)2；
Compound E:M1=M2=M3=M4=M5=M6=OCH2CH2CH2CH3；
Compound F:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH3；
Compound G:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH3；
Compound H:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH2CH3；
Compound I:M1=M2=M3=M4=M5=M6=OH；
Compound J:M1=M3=M5=OCH3；M2=M4=M6=OH；
Compound K: M1=M3=M5=OCH3；M2=M4=M6=NH2；
Compound L: M1=M3=M5=OCH3；M2=M4=M6=Cl；
Compound M:M1=M3=M5=OCH3；M2=M4=M6=Br；
Compound N: M1=M3=M5=OCH3；M2=M4=M6=I；
Compound O:M1=M3=M5=OCH3；M2=M4=M6=CHO；
Compound P:M1=M3=M5=OCH3；M2=M4=M6=OCH2CH2CH2Br；
Compound Q: M1=M2=M3=M4=M5=M6=OCH2CH2Cl。
4. catalyst system according to claim 1, wherein the general formula of the alkoxyl magnesium compound is Mg (OR3)a
(OR4)2-a, R3And R4Respectively substituted or unsubstituted C1~C10Alkyl, substituent group be hydroxyl, amino, aldehyde radical, carboxyl, acyl group,
Halogen atom, alkoxy or hetero atom, 0≤a≤2.
5. catalyst system according to claim 1, wherein the general formula of the titanium compound is Ti (OR2)nX2 4-n,
In, R2For C1~C8Alkyl, preferably C1~C8Alkyl；X2For Cl, Br or I, 0≤n≤4；
Preferably, the titanium compound is selected from TiCl4、Ti(OC2H5)Cl3、Ti(OCH3)Cl3、Ti(OC4H9)Cl3And Ti
(OC4H9)4At least one of.
6. catalyst system according to claim 1, wherein in the ingredient of solid catalyst, in terms of every mole of magnesium, institute
The dosage for stating titanium compound is 0.1~15mol；The dosage of the internal electron donor compound is 0~0.1mol.
7. catalyst system according to claim 1, wherein the organo-aluminum compound is selected from Al (CH2CH3)3、Al(i-
Bu)3With Al (n-C6H13)3At least one of.
8. catalyst system according to claim 1, wherein aluminium and the solid catalysis in the organo-aluminum compound
The molar ratio of titanium in agent component is 5 ︰, 1~500 ︰ 1,1~200 ︰ 1 of preferably 20 ︰.
9. catalyst system according to claim 1, wherein the external donor compound and the solid catalyst
The molar ratio of titanium is 0.5 ︰, 1~50 ︰ 1 in component.
10. caltalyst described in any one of claim 1~9 ties up to the application in olefin polymerization.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710591181.3A CN109280103B (en) | 2017-07-19 | 2017-07-19 | Catalyst system for olefin polymerization and application thereof |
| RU2020103744A RU2740916C1 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerisation catalyst comprising cyclotriveratrilene and derivatives thereof |
| US16/631,482 US11401356B2 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst comprising cyclotriveratrylene and derivatives thereof |
| KR1020207002897A KR102336976B1 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst comprising cyclotiberatrylene and derivatives thereof |
| PCT/CN2018/096248 WO2019015638A1 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst comprising cyclotriveratrylene and derivatives thereof |
| CN201880002860.5A CN109526217B (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst containing cyclotri veratrum hydrocarbon and derivatives thereof |
| JP2020502696A JP7038797B2 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst containing cyclotribellatrilen and its derivatives |
| EP18835679.4A EP3656754A4 (en) | 2017-07-19 | 2018-07-19 | Olefin polymerization catalyst comprising cyclotriveratrylene and derivatives thereof |
| BR112020001201-7A BR112020001201B1 (en) | 2017-07-19 | 2018-07-19 | ZIEGLER-NATTA CATALYST SYSTEM FOR OLEFIN POLYMERIZATION, SOLID CATALYST COMPONENT FOR OLEFIN POLYMERIZATION AND OLEFIN POLYMERIZATION PROCESS |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710591181.3A CN109280103B (en) | 2017-07-19 | 2017-07-19 | Catalyst system for olefin polymerization and application thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109280103A true CN109280103A (en) | 2019-01-29 |
| CN109280103B CN109280103B (en) | 2021-02-05 |
Family
ID=65185026
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710591181.3A Active CN109280103B (en) | 2017-07-19 | 2017-07-19 | Catalyst system for olefin polymerization and application thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109280103B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110734510A (en) * | 2018-07-19 | 2020-01-31 | 中国石油化工股份有限公司 | Olefin polymerization catalyst containing cyclotri veratrum hydrocarbon and its derivatives |
| CN113004452A (en) * | 2021-04-27 | 2021-06-22 | 辛集市旭远新材料科技有限公司 | Impact-resistant polypropylene and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1272851A (en) * | 1998-06-16 | 2000-11-08 | 三井化学株式会社 | Catalyst for olefin polymerization and method of polymerizing olefin |
| US6255419B1 (en) * | 1997-02-07 | 2001-07-03 | Mitsui Chemicals, Inc. | Olefin polymerization catalyst and process for producing olefin polymers |
| CN103509218A (en) * | 2012-06-18 | 2014-01-15 | 中国石油化工股份有限公司 | Components of catalyst used for olefin polymerization and preparation method thereof |
| WO2015091984A1 (en) * | 2013-12-20 | 2015-06-25 | Saudi Basic Industries Corporation | Procatalyst for polymerization of olefins |
-
2017
- 2017-07-19 CN CN201710591181.3A patent/CN109280103B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6255419B1 (en) * | 1997-02-07 | 2001-07-03 | Mitsui Chemicals, Inc. | Olefin polymerization catalyst and process for producing olefin polymers |
| CN1272851A (en) * | 1998-06-16 | 2000-11-08 | 三井化学株式会社 | Catalyst for olefin polymerization and method of polymerizing olefin |
| CN103509218A (en) * | 2012-06-18 | 2014-01-15 | 中国石油化工股份有限公司 | Components of catalyst used for olefin polymerization and preparation method thereof |
| WO2015091984A1 (en) * | 2013-12-20 | 2015-06-25 | Saudi Basic Industries Corporation | Procatalyst for polymerization of olefins |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110734510A (en) * | 2018-07-19 | 2020-01-31 | 中国石油化工股份有限公司 | Olefin polymerization catalyst containing cyclotri veratrum hydrocarbon and its derivatives |
| CN110734510B (en) * | 2018-07-19 | 2022-02-08 | 中国石油化工股份有限公司 | Olefin polymerization catalyst containing cyclotri veratrum hydrocarbon and its derivatives |
| CN113004452A (en) * | 2021-04-27 | 2021-06-22 | 辛集市旭远新材料科技有限公司 | Impact-resistant polypropylene and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109280103B (en) | 2021-02-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109280101A (en) | Ingredient of solid catalyst and catalyst system and olefine polymerizing process for olefinic polymerization | |
| CN110016094B (en) | Solid catalyst component and catalyst system for olefin polymerization and olefin polymerization process | |
| WO2015055137A1 (en) | Catalyst component for olefin polymerization, preparation method thereof, and catalyst comprising same | |
| CN109280102B (en) | Solid catalyst component and catalyst system for olefin polymerization and olefin polymerization process | |
| CN110016093A (en) | Ingredient of solid catalyst and catalyst system and olefine polymerizing process for olefinic polymerization | |
| CN109280110A (en) | For the ingredient of solid catalyst and olefin polymerization catalysis of olefinic polymerization and its application and ethylene copolymer | |
| CN106170500A (en) | Catalytic component for olefinic polymerization | |
| CN109280104A (en) | Application of the three black false hellebore hydrocarbons and their derivates of ring in olefin polymerization catalysis | |
| EP4038108A1 (en) | Process for polymerization of polypropylene using ziegler-natta procatalyst with novel 1,3-diether internal electron donors | |
| CN109280106A (en) | Ingredient of solid catalyst and catalyst system and olefine polymerizing process for olefinic polymerization | |
| CN109280103A (en) | A kind of catalyst system and its application for olefinic polymerization | |
| CN109526217A (en) | Olefin polymerization catalysis comprising three black false hellebore hydrocarbons and their derivates of ring | |
| CN104558281A (en) | Spherical carrier used for olefin polymerization catalyst and preparation method thereof | |
| CN109280111A (en) | A kind of catalyst system and its application for olefinic polymerization | |
| CN109280109A (en) | A kind of catalyst system and its application for olefinic polymerization | |
| CN109280107A (en) | A kind of catalyst system and its application for olefinic polymerization | |
| CN111234064B (en) | Solid catalyst component for olefin polymerization, olefin polymerization catalyst and application thereof | |
| CN110734510A (en) | Olefin polymerization catalyst containing cyclotri veratrum hydrocarbon and its derivatives | |
| CN109280105A (en) | A kind of catalyst system and its application for olefinic polymerization | |
| CN102453152A (en) | Olefin polymerization catalyst system and olefin polymerization method using same | |
| CN110016096B (en) | Catalyst carrier for olefin polymerization and preparation method thereof, solid catalyst component, catalyst system and olefin polymerization method | |
| CN109280108A (en) | Ingredient of solid catalyst and catalyst system and olefine polymerizing process for olefinic polymerization | |
| CN107987196A (en) | For catalyst constituent for olefinic polymerization and its catalyst | |
| CN113754801B (en) | Solid catalyst for preparing olefin polymer and solid catalyst system | |
| CN100491386C (en) | Multinuclear metallocene complex and application thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |