CN102399322A - Load-type non-metallocene catalyst, preparation method thereof, and application thereof - Google Patents

Abstract

The invention relates to a load-type non-metallocene catalyst and a preparation method thereof. The load-type non-metallocene catalyst is characterized by simple and feasible preparation technology, controllable non-metallocene content, substantial copolymerization effect, and the like. The invention also relates to an application of the load-type non-metallocene catalyst in alkene homopolymerization/copolymerization. Compared to prior arts, the application is characterized by high alkene polymerization catalytic activity, high polymer bulk density, and controllable molecular weight distribution.

Description

Load type non-metallocene catalyst, its preparation method and application thereof

Technical field

The present invention relates to a kind of non-metallocene catalyst.Particularly, the present invention relates to a kind of load type non-metallocene catalyst, its preparation method and the application in alkene homopolymerization/copolymerization thereof.

Background technology

The non-metallocene catalyst that middle and later periods nineteen nineties occurs; Claim luxuriant rear catalyst again; The central atom of Primary Catalysts has comprised nearly all transition metal; Reach at some aspect of performance, even surpass metallocene catalyst, become after Ziegler, Ziegler-Natta and metallocene catalyst the 4th generation olefin polymerization catalysis.By the excellent property of the polyolefin products of such catalyzer manufacturing, and low cost of manufacture.The non-metallocene catalyst ligating atom is oxygen, nitrogen, sulphur and phosphorus; Do not contain cyclopentadienyl group or its deriveding group,, it is characterized in that central ion has stronger Electron Affinities like indenyl and fluorenyl etc.; And have cis alkyl or halogen metal division center; Carry out alkene insertion and σ-key easily and shift, the easy alkylation of central metal helps the generation at cation activity center; The title complex that forms has the geometric configuration of qualification, stereoselectivity, electronegativity and chirality controllability, and in addition, formed metal-carbon key polarizes easily, more helps the polymerization and the copolymerization of alkene.Therefore, even under higher polymeric reaction temperature, also can obtain the olefin polymer of higher molecular weight.

But homogeneous catalyst has been proved it in olefinic polyreaction has the active duration weak point, glue still easily, promotor MAO consumption is high; And obtain the too low or too high weak point of polymericular weight; Only might be applied to the solution polymerization process or the high-pressure polymerization process of alkene, seriously limit its industrial applicability.

Patent ZL 01126323.7, ZL 02151294.9ZL 02110844.7 and WO 03/010207 disclose a kind of alkene homopolymerization/catalyst for copolymerization or catalystsystem; Has alkene homopolymerization/copolymerization performance widely; But need higher promotor consumption during in olefinic polymerization at the disclosed catalyzer of this patent or catalystsystem; Could obtain suitable olefin polymerizating activity, and it is short to exist active duration in the polymerization process, phenomenons such as the sticking still of polymkeric substance.

Common way is that non-metallocene catalyst is technological through certain loadization, processes loaded catalyst, thereby improves the polymerization of alkene and the particle form of resulting polymers.It shows as the initial activity that has suitably reduced catalyzer to a certain extent; Prolong the polymerization activity life-span of catalyzer; Reduce even avoided the caking in the polymerization process or gathered phenomenon cruelly, improve the form of polymkeric substance, improve the apparent density of polymkeric substance; Can make it satisfy more polymerization technique process, like vapour phase polymerization or slurry polymerization etc.

To patent ZL 01126323.7, ZL 02151294.9ZL 02110844.7 and the disclosed non-metallocene catalyst of WO03/010207; Patent CN200310106156.x, CN200310106157.4, CN200410066070.3, CN200410066069.0,200510119401.x etc. provide multiple mode to carry out load to obtain load type non-metallocene catalyst; But these patents all relate to the Nonmetallocene organic cpds that contains transition metal are carried on the carrier after the processing, and catalyst preparation process is comparatively complicated.

The catalyzer that with the Magnesium Chloride Anhydrous is carrier demonstrates advantages of high catalytic activity in olefin polymerization process, but this type of catalyst strength is poor, and is broken easily in polymerization reactor, thereby causes polymer morphology bad.Silicon dioxide carried catalyzer has good flowability, can be used for slurry polymerization and gas fluidised bed polymerisation, but adopts silicon dioxide carried metallocene and non-metallocene catalyst then to show lower catalytic activity merely.Therefore, just possibly prepare and have high catalytic activity, the catalyzer of the controlled and good abrasion strength resistance of globule size if magnesium chloride and silicon-dioxide are well organically combined.

Patent 200610026765.8 discloses one type of single active center's Z-N olefin polymerization catalysis.This catalyzer as electron donor, handles through pretreated carrier (like silica gel), metallic compound (like titanium tetrachloride) and electron donor through in magnesium compound (like magnesium chloride)/tetrahydrofuran solution, adding that the back obtains with the salicylic alidehyde imine that contains coordinating group or substituted salicylic alidehyde imine verivate.

Patent 200610026766.2 is similar with it, discloses one type and has contained heteroatomic organic cpds and the application in Ziegler-Natta catalyst thereof.

Patent 200910180601.4 discloses a kind of preparation method of load type non-metallocene catalyst; It is that magnesium compound and Nonmetallocene title complex are dissolved in the solvent; Add porous support after drying, obtain load type non-metallocene catalyst through thermal activation treatment.Patent 200910180606.7 discloses a kind of preparation method of load type non-metallocene catalyst; It is that magnesium compound and Nonmetallocene title complex are dissolved in the solvent; Add through behind the porous support of thermal activation treatment; It is dry to add the washing of precipitation agent after-filtration again, obtains load type non-metallocene catalyst.What these two kinds of methods were all used is the porous support that thermal activation treatment is crossed; Though porous support through thermal activation treatment, dewaters and dehydroxylation, still contains the free hydroxyl of more amount on the surface; Follow-up load non-metallocene metal complexes is had a negative impact, limited its active performance.

Chinese patent 200910180100.6,200910180607.1,200910210988.3,200910210984.5,200910210987.9,200910210991.5 disclosed load type non-metallocene catalyst preparing methods and above-mentioned patent are similar; What all use is thermal activation treatment porous support of crossing and the magnesium compound solution reaction that contains Nonmetallocene part or Nonmetallocene title complex; React with the chemical processing agent that contains IVB family metallic compound more at last, obtain load type non-metallocene catalyst.

Chinese patent 200910180602.9 discloses a kind of preparation method of load type non-metallocene catalyst, and it is that magnesium compound and Nonmetallocene title complex are dissolved in the solvent, obtains load type non-metallocene catalyst after the drying.Patent 200910180605.2 discloses a kind of preparation method of load type non-metallocene catalyst, and it is that magnesium compound and Nonmetallocene title complex are dissolved in the solvent, adds the precipitation agent deposition, obtains load type non-metallocene catalyst after the filtration washing drying.What these two kinds of methods adopted is the magnesium compound carrier, the particle form of catalyzer is difficult to control, has limited the polymer beads form that polymerization thus obtains.

Patent 200910180603.3,200910180604.8,200910210989.8,200910210986.4,200910210985.X, 200910210990.0 disclosed load type non-metallocene catalyst preparing methods and above-mentioned patent are similar; What all use is that magnesium compound is as carrier; Still exist the particle form of catalyzer to be difficult to control, limited the polymer beads form that polymerization thus obtains.

Even so; The ubiquitous problem of load type non-metallocene catalyst of the prior art is; The load process is complicated, load non-metallocene metal complexes again after the multistep that generally need carry out carrier is handled, and olefin polymerizating activity is low and be difficult to regulate; And, when carrying out olefinic polymerization, must assist with higher promotor consumption in order to improve its polymerization activity.For the carrier loaded non-metallocene catalyst of porous support list; Carrier needs after thermal activation treatment to handle with the chemical reagent of its reaction with aluminum alkyls etc. again; Need strict control preparation condition for the carrier loaded non-metallocene catalyst of magnesium compound list, these two kinds of methods all are difficult to obtain good form polymkeric substance through olefinic polymerization.And the composite carrier load non-metallocene catalyst that forms for porous support and magnesium compound; Such as Chinese patent 200410066068.6; And based on load method and a kind of carry type non-metallocene calalyst for polymerization of olefine, its preparation method and the application thereof of the disclosed a kind of high reactivity non-metallocene catalyst of the patent PCT/CN2005/001737 of its application, it is with carrier and chemical activating agent (titanium tetrachloride etc.) effect, obtains modifying carrier; Join in the THF-alcoholic solution of magnesium compound; Filtration washing, drying and drain back and Nonmetallocene complex solution reaction, washing and filtering, vacuum-drying make load type non-metallocene catalyst.This load method is comparatively complicated; Process is difficult to control; The factor of influence batch quality is more, is unfavorable for extensive use, and because the existence of alcohol in the system; Can have a negative impact to load non-metallocene catalyst performance on it, limit the performance of non-metallocene catalyst intrinsic performance.

Therefore, present present situation is, still needs a kind of load type non-metallocene catalyst, and its preparation method is simple, is fit to suitability for industrialized production, and can overcomes those problems that exist in the prior art load type non-metallocene catalyst.

Summary of the invention

The inventor through diligent discovering, makes said load type non-metallocene catalyst through using a kind of specific preparation method on the basis of existing technology, just can solve foregoing problems, and accomplish the present invention thus.

According to the preparation method of this load type non-metallocene catalyst, need not add proton donor and electron donor (such as in this area for this reason and the conventional diether compounds that uses) etc., also need not harsh reaction requirement and reaction conditions.Therefore, the preparation method of this loaded catalyst is simple, and is very suitable for suitability for industrialized production.

Particularly, the present invention relates to the content of following aspect:

1. the preparation method of a load type non-metallocene catalyst may further comprise the steps:

Make the chemical processing agent and optional porous support reaction, the step that obtains to modify carrier that are selected from IV B family metallic compound through thermal activation treatment;

Magnesium compound is dissolved in the solvent, obtains the step of magnesium compound solution;

Said modification carrier, said magnesium compound solution are contacted with the Nonmetallocene title complex, obtain the step of mixed serum;

The said mixed serum of convection drying, the step of acquisition complex carrier; With

Make the chemical processing agent and the reaction of said complex carrier that are selected from said IV B family metallic compound, obtain the step of said load type non-metallocene catalyst.

2. according to the aforementioned described preparation method in arbitrary aspect, also be included in and make before said chemical processing agent and the reaction of said complex carrier, with the step that helps the said complex carrier of chemical processing agent pre-treatment that is selected from aikyiaiurnirsoxan beta, aluminum alkyls or its arbitrary combination.

3. according to the aforementioned described preparation method in arbitrary aspect; It is characterized in that; Said porous support is selected from the refractory oxide or in infusibility composite oxides, clay, molecular sieve, mica, polynite, wilkinite and the zeyssatite one or more of partial cross-linked form, periodic table of elements II A, III A, IV A or the IV B family metal of olefin homo or multipolymer, Z 150PH or its multipolymer, Schardinger dextrins, polyester or copolyesters, polymeric amide or copolyamide, ryuron or multipolymer, Voncoat R 3310 or multipolymer, methylacrylic acid ester homopolymer or multipolymer, styrene homopolymers or multipolymer, these homopolymer or multipolymer; Be preferably selected from partial cross-linked styrene polymer, silicon-dioxide, aluminum oxide, Natural manganese dioxide, oxidation sial, oxidation magnalium, titanium oxide, molecular sieve and the polynite one or more, more preferably be selected from silicon-dioxide.

4. according to the aforementioned described preparation method in arbitrary aspect; It is characterized in that; Said magnesium compound is selected from one or more in magnesium halide, alkoxyl group magnesium halide, alkoxyl magnesium, alkyl magnesium, alkyl halide magnesium and the alkyl alkoxy magnesium; Be preferably selected from the magnesium halide one or more, more preferably magnesium chloride.

5. according to the aforementioned described preparation method in arbitrary aspect, it is characterized in that said solvent is selected from C _6-12Aromatic hydrocarbon, halo C _6-12In aromatic hydrocarbon, ester and the ether one or more are preferably selected from C _6-12In aromatic hydrocarbon and the THF one or more, most preferably THF.

6. according to the aforementioned described preparation method in arbitrary aspect, it is characterized in that said Nonmetallocene title complex is selected from one or more in the compound with following chemical structural formula:

Be preferably selected from compound (A) with following chemical structural formula and in the compound (B) one or more:

More preferably be selected from compound (A-1) to compound (A-4) with following chemical structural formula and in compound (B-1) to the compound (B-4) one or more:

In above all chemical structural formulas,

Q is 0 or 1;

D is 0 or 1;

M is 1,2 or 3;

M is selected from periodic table of elements III family to XI family atoms metal, preferred IV B family atoms metal, more preferably Ti (IV) and Zr (IV);

N is 1,2,3 or 4, depends on the valence state of said central metal atom M;

X is selected from halogen, Wasserstoffatoms, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, nitrogen-containing group, sulfur-containing group, boron-containing group, contain aluminium base group, phosphorus-containing groups, silicon-containing group, germanic group or contain tin group, a plurality of X can be identical, also can be different, can also become key or Cheng Huan each other;

A be selected from Sauerstoffatom, sulphur atom, selenium atom,

-NR ²³R ²⁴,-N (O) R ²⁵R ²⁶,

-PR ²⁸R ²⁹,-P (O) R ³⁰OR ³¹, sulfuryl, sulfoxide group or-Se (O) R ³⁹, wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

B is selected from nitrogen-atoms, nitrogen-containing group, phosphorus-containing groups or C ₁-C ₃₀Alkyl;

D is selected from nitrogen-atoms, Sauerstoffatom, sulphur atom, selenium atom, phosphorus atom, nitrogen-containing group, phosphorus-containing groups, C ₁-C ₃₀Alkyl, sulfuryl, sulfoxide group,

-N (O) R ²⁵R ²⁶,

Or-P (O) R ³²(OR ³³), wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

E is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

F is selected from nitrogen-atoms, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

G is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Y is selected from Sauerstoffatom, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

Z is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

→ represent singly-bound or two key;

-represent covalent linkage or ionic linkage;

---represent co-ordination bond, covalent linkage or ionic linkage;

R ¹To R ⁴, R ⁶To R ³⁶, R ³⁸And R ³⁹Be selected from hydrogen, C independently of one another ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group, above-mentioned group can be the same or different to each other, and wherein adjacent group can combine togather into key or Cheng Huan, is preferably formed aromatic ring, and

R ⁵Be selected from lone-pair electron on the nitrogen, hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, sulfur-containing group, nitrogen-containing group, contain seleno group or phosphorus-containing groups; Work as R ⁵For oxy radical, sulfur-containing group, nitrogen-containing group, when containing seleno group or phosphorus-containing groups, R ⁵In N, O, S, P and Se can be used as coordination and carry out coordination with atom and said center IV B family atoms metal,

Said Nonmetallocene title complex further is preferably selected from one or more in the compound with following chemical structural formula:

Most preferably be selected from the compound with following chemical structural formula one or more:

7. according to the aforementioned described preparation method in arbitrary aspect, it is characterized in that,

Said halogen is selected from F, Cl, Br or I;

Said nitrogen-containing group is selected from

-NR ²³R ²⁴,-T-NR ²³R ²⁴Or-N (O) R ²⁵R ²⁶

Said phosphorus-containing groups is selected from

-PR ²⁸R ²⁹,-P (O) R ³⁰R ³¹Or-P (O) R ³²(OR ³³);

Said oxy radical be selected from hydroxyl ,-OR ³⁴With-T-OR ³⁴

Said sulfur-containing group is selected from-SR ³⁵,-T-SR ³⁵,-S (O) R ³⁶Or-T-SO ₂R ³⁷

The said seleno group that contains is selected from-SeR ³⁸,-T-SeR ³⁸,-Se (O) R ³⁹Or-T-Se (O) R ³⁹

Said group T is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Said R ³⁷Be selected from hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Said C ₁-C ₃₀Alkyl is selected from C ₁-C ₃₀Alkyl, C ₇-C ₅₀Alkaryl, C ₇-C ₅₀Aralkyl, C ₃-C ₃₀Cyclic alkyl, C ₂-C ₃₀Thiazolinyl, C ₂-C ₃₀Alkynyl, C ₆-C ₃₀Aryl, C ₈-C ₃₀Condensed ring radical or C ₄-C ₃₀Heterocyclic radical, wherein said heterocyclic radical contain 1-3 heteroatoms that is selected from nitrogen-atoms, Sauerstoffatom or sulphur atom;

Said substituted C ₁-C ₃₀Alkyl is selected from and has one or more aforementioned halogens or aforementioned C ₁-C ₃₀Alkyl is as substituent aforementioned C ₁-C ₃₀Alkyl;

Said safing function property group is selected from aforementioned halogen, aforementioned oxy radical, aforementioned nitrogen-containing group, silicon-containing group, germanic group, aforementioned sulfur-containing group, contains tin group, C ₁-C ₁₀Ester group or nitro,

Wherein, said boron-containing group is selected from BF ₄ ^-, (C ₆F ₅) ₄B ^-Or (R ⁴⁰BAr ₃) ^-

Saidly contain aluminium base group and be selected from aluminum alkyls, AlPh ₄ ^-, AlF ₄ ^-, AlCl ₄ ^-, AlBr ₄ ^-, AlI ₄ ^-Or R ⁴¹AlAr ₃ ^-

Said silicon-containing group is selected from-SiR ⁴²R ⁴³R ⁴⁴Or-T-SiR ⁴⁵

Said germanic group is selected from-GeR ⁴⁶R ⁴⁷R ⁴⁸Or-T-GeR ⁴⁹

Saidly contain tin group and be selected from-SnR ⁵⁰R ⁵¹R ⁵²,-T-SnR ⁵³Or-T-Sn (O) R ⁵⁴,

Said Ar represents C ₆-C ₃₀Aryl, and

R ⁴⁰To R ⁵⁴Be selected from hydrogen, aforementioned C independently of one another ₁-C ₃₀Alkyl, aforementioned substituted C ₁-C ₃₀Alkyl or aforementioned safing function property group, wherein these groups can be the same or different to each other, and wherein adjacent group can combine togather into key or Cheng Huan, and said group T ditto defines.

8. according to the aforementioned described preparation method in arbitrary aspect, it is characterized in that, is 1 in the said magnesium compound of Mg element and the mol ratio of said Nonmetallocene title complex: 0.01-1; Preferred 1: 0.04-0.4, more preferably 1: 0.08-0.2, the ratio of said magnesium compound and said solvent is 1mol: 75～400ml; Preferred 1mol: 150～300ml; More preferably 1mol: 200～250ml is 1 in the said magnesium compound of magnesium compound solid and the mass ratio of said porous support: 0.1-20, preferred 1: 0.5-10; More preferably 1: 1-5; And is respectively 1 in the said magnesium compound of Mg element independently of one another with mol ratio in the said chemical processing agent of IV B family metallic element: 0.01-1, preferred 1: 0.01-0.50, more preferably 1: 0.10-0.30.

9. according to the aforementioned described preparation method in arbitrary aspect; It is characterized in that; Said IV B family metallic compound is selected from one or more in IV B family metal halide, IV B family metal alkyl compound, IV B family metal alkoxide compound, IV B family metal alkyl halides and the IV B family metal alkoxide halogenide; Be preferably selected from the IV B family metal halide one or more, more preferably be selected from TiCl ₄, TiBr ₄, ZrCl ₄, ZrBr ₄, HfCl ₄And HfBr ₄In one or more, most preferably be selected from TiCl ₄And ZrCl ₄In one or more.

10. according to the aforementioned described preparation method in arbitrary aspect; It is characterized in that; Said aikyiaiurnirsoxan beta is selected from one or more in MAO, ethyl aikyiaiurnirsoxan beta, isobutyl aluminium alkoxide and the normal-butyl alumina alkane; More preferably be selected from MAO and the isobutyl aluminium alkoxide one or more; And said aluminum alkyls is selected from trimethylaluminium, triethyl aluminum, tri-propyl aluminum, triisobutyl aluminium, three n-butylaluminum, triisopentyl aluminium, three n-pentyl aluminium, three hexyl aluminium, three isohexyl aluminium, diethylmethyl aluminium and the dimethyl ethyl aluminium one or more; Be preferably selected from trimethylaluminium, triethyl aluminum, tri-propyl aluminum and the triisobutyl aluminium one or more, most preferably be selected from triethyl aluminum and the triisobutyl aluminium one or more.

It 11., it is characterized in that, is 1 with helping the mol ratio of chemical processing agent: 0-1.0, preferred 1: 0-0.5, more preferably 1: 0.1-0.5 in Al element said in the said magnesium compound of Mg element according to the aforementioned described preparation method in arbitrary aspect.

12. a load type non-metallocene catalyst, it is by making according to each described preparation method of aspect 1-11.

13. alkene homopolymerization/copolymerization process; It is characterized in that; Being Primary Catalysts according to aspect 12 described load type non-metallocene catalysts; To be selected from aikyiaiurnirsoxan beta, aluminum alkyls, haloalkyl aluminium, boron fluothane, boron alkyl and the boron alkyl ammonium salt one or more is promotor, makes alkene homopolymerization or copolymerization.

14. an alkene homopolymerization/copolymerization process is characterized in that, may further comprise the steps:

According to each described preparation method of aspect 1-11 make load type non-metallocene catalyst and

With said load type non-metallocene catalyst is Primary Catalysts, is promotor to be selected from aikyiaiurnirsoxan beta, aluminum alkyls, haloalkyl aluminium, boron fluothane, boron alkyl and the boron alkyl ammonium salt one or more, makes alkene homopolymerization or copolymerization.

Technique effect

Preparing method's technology simple possible of load type non-metallocene catalyst of the present invention; And the charge capacity of Nonmetallocene title complex is adjustable; Can give full play to it and obtain the performance of polyolefin product at catalysis in olefine polymerization, and the polymerization catalyst activity is higher, polymer stacks density is also higher.

Method for preparing catalyst provided by the invention and resulting thus load type non-metallocene catalyst; Wherein the Nonmetallocene title complex has the effect of the molecular weight distribution of narrowing; Chemical processing agent has the MWD and the effectiveness that improves polymer stacks density of wide fluidized polymer, therefore can be through regulating the MWD that the relative proportioning with the complex carrier chemical processing agent of Nonmetallocene title complex is come telomerized polymer.

And, when employing load type non-metallocene catalyst that the present invention obtained and promotor constitute catalystsystem, show significant comonomer effect during copolymerization, promptly under equal relatively condition, the copolymerization activity is higher than the homopolymerization activity.

Also find simultaneously, in catalyst preparation process, introduce the effect that helps chemical processing agent to have the increase catalyst activity and the molecular weight distribution that narrows.

Embodiment

Following specific embodiments of the invention is elaborated, but it is pointed out that protection scope of the present invention does not receive the restriction of these embodiments, but is confirmed by claims of appendix.

The present invention relates to a kind of preparation method of load type non-metallocene catalyst, may further comprise the steps: make the chemical processing agent and optional porous support reaction, the step that obtains to modify carrier that are selected from IV B family metallic compound through thermal activation treatment; Magnesium compound is dissolved in the solvent, obtains the step of magnesium compound solution; Said modification carrier, said magnesium compound solution are contacted with the Nonmetallocene title complex, obtain the step of mixed serum; The said mixed serum of convection drying, the step of acquisition complex carrier; With make chemical processing agent and the reaction of said complex carrier that is selected from said IV B family metallic compound, obtain the step of said load type non-metallocene catalyst.

Below said porous support is carried out bright specifically.

According to the present invention, as said porous support, such as can enumerate this area when making supported olefin polymerization catalyst as carrier and conventional those organic or inorganic porosu solids that use.

Particularly; As said organic porosu solid; Such as enumerating olefin homo or multipolymer, Z 150PH or its multipolymer, Schardinger dextrins, (being total to) polyester, (being total to) polymeric amide, ryuron or multipolymer, Voncoat R 3310 or multipolymer, methylacrylic acid ester homopolymer or multipolymer; And styrene homopolymers or multipolymer etc.; And the partial cross-linked form of these homopolymer or multipolymer, wherein preferably partial cross-linked (such as degree of crosslinking be at least 2% but less than 100%) styrene polymer.

Embodiment preferred according to the present invention; Preferably on the surface of said organic porosu solid, have such as any one or the multiple active function groups that are selected from hydroxyl, primary amino, secondary amino group, sulfonic group, carboxyl, carboxamido-group, the mono-substituted carboxamido-group of N-, sulfoamido, the mono-substituted sulfoamido of N-, sulfydryl, acylimino and the hydrazide group wherein preferred carboxyl and hydroxyl.

According to an embodiment of the invention, before use said organic porosu solid is carried out thermal activation treatment.This thermal activation treatment can be carried out according to common mode, such as under reduced pressure or under the inert atmosphere said organic porosu solid being carried out heat treated.Here said inert atmosphere be meant only contain extremely trace in the gas or do not contain can with the component of said organic porosu solid reaction.As said inert atmosphere, such as enumerating nitrogen or rare gas atmosphere, nitrogen atmosphere.Because the poor heat resistance of organic porosu solid, so this thermal activation process is with the structure of not destroying said organic porosu solid itself with basic composition is prerequisite.Usually, the temperature of this thermal activation is 50～400 ℃, preferred 100～250 ℃, and the thermal activation time is 1～24h, preferred 2～12h.After the thermal activation treatment, said organic porosu solid need be preserved subsequent use in malleation under the inert atmosphere.

As said inorganic porous solid; Such as the refractory oxide that can enumerate periodic table of elements II A, III A, IV A or IV B family metal (such as silicon-dioxide (being called silicon oxide or silica gel again), aluminum oxide, Natural manganese dioxide, titanium oxide, zirconium white or Thorotrast etc.); Perhaps any infusibility composite oxides of these metals (such as oxidation sial, oxidation magnalium, titanium oxide silicon, titanium oxide magnesium and titanium oxide aluminium etc.), and clay, molecular sieve (such as ZSM-5 and MCM-41), mica, polynite, wilkinite and zeyssatite etc.As said inorganic porous solid, can also enumerate the oxide compound that generates through pyrohydrolysis by gaseous metal halogenide or gaseous silicon compound, such as the silica gel that obtains by the silicon tetrachloride pyrohydrolysis, the aluminum oxide that perhaps obtains etc. by the aluminum chloride pyrohydrolysis.

As said inorganic porous solid, preferred silicon-dioxide, aluminum oxide, Natural manganese dioxide, oxidation sial, oxidation magnalium, titanium oxide silicon, titanium oxide, molecular sieve and polynite etc., preferred especially silicon-dioxide.

According to the present invention; Suitable silicon-dioxide can pass through the ordinary method manufacturing; It perhaps can be the commerical prod that to buy arbitrarily; Such as the Grace that can enumerate Grace company 955, Grace948, Grace SP9-351, Grace SP9-485, Grace SP9-10046, Davsion Syloid 245 and Aerosil812, the ES70 of Ineos company, ES70X, ES70Y, ES70W, ES757, EP10X and EP11, and CS-2133 of Pq Corp. and MS-3040.

Embodiment preferred according to the present invention preferably has hydroxyl isoreactivity functional group on said inorganic porous solid surface.

According to the present invention, in one embodiment, before use said inorganic porous solid is carried out thermal activation treatment.This thermal activation treatment can be carried out according to common mode, such as under reduced pressure or under the inert atmosphere said inorganic porous solid being carried out heat treated.Here said inert atmosphere be meant only contain extremely trace in the gas or do not contain can with the component of said inorganic porous solid reaction.As said inert atmosphere, such as enumerating nitrogen or rare gas atmosphere, nitrogen atmosphere.Usually, the temperature of this thermal activation is 200-800 ℃, and preferred 400～700 ℃, most preferably 400～650 ℃, heat-up time is such as being 0.5～24h, preferred 2～12h, most preferably 4～8h.After the thermal activation treatment, said inorganic porous solid need be preserved subsequent use in malleation under the inert atmosphere.

According to the present invention, the surface-area of said porous support is not had special qualification, but be generally 10～1000m ²/ g (BET method mensuration), preferred 100～600m ²/ g; The pore volume of this porous support (determination of nitrogen adsorption) is generally 0.1～4cm ³/ g, preferred 0.2～2cm ³/ g, and preferred 1～500 μ m of its median size (laser particle analyzer mensuration), more preferably 1～100 μ m.

According to the present invention, said porous support can be a form arbitrarily, such as micropowder, granular, spherical, aggregate or other form.

Below said chemical processing agent is carried out bright specifically.

According to the present invention, with IV B family metallic compound as said chemical processing agent.

As said IV B family metallic compound, such as enumerating IV B family metal halide, IV B family metal alkyl compound, IV B family metal alkoxide compound, IV B family metal alkyl halides and IV B family metal alkoxide halogenide.

As said IV B family metal halide, said IV B family metal alkyl compound, said IV B family metal alkoxide compound, said IV B family's metal alkyl halides and said IV B family metal alkoxide halogenide, such as the compound that can enumerate following logical formula IV structure:

M(OR ¹) _mX _nR ² _4-m-n (Ⅳ)

Wherein:

M is 0,1,2,3 or 4;

N is 0,1,2,3 or 4;

M is an IV B family metal in the periodic table of elements, such as titanium, zirconium and hafnium etc.;

X is a halogen, such as F, Cl, Br and I etc.; And

R ¹And R ²Be selected from C independently of one another _1-10Alkyl is such as methyl, ethyl, propyl group, normal-butyl, isobutyl-etc., R ¹And R ²Can be identical, also can be different.

Particularly, as said IV B family metal halide, such as enumerating titanium tetrafluoride (TiF ₄), titanium tetrachloride (TiCl ₄), titanium tetrabromide (TiBr ₄), titanium tetra iodide (TiI ₄);

Zirconium tetrafluoride (ZrF ₄), zirconium tetrachloride (ZrCl ₄), tetrabormated zirconium (ZrBr ₄), zirconium tetraiodide (ZrI ₄);

Tetrafluoride hafnium (HfF ₄), hafnium tetrachloride (HfCl ₄), hafnium (HfBr ₄), tetraiodide hafnium (HfI ₄).

As said IV B family metal alkyl compound, such as enumerating tetramethyl-titanium (Ti (CH ₃) ₄), tetraethyl-titanium (Ti (CH ₃CH ₂) ₄), four isobutyl-titanium (Ti (i-C ₄H ₉) ₄), tetra-n-butyl titanium (Ti (C ₄H ₉) ₄), triethyl methyltitanium (Ti (CH ₃) (CH ₃CH ₂) ₃), diethyl-dimethyl titanium (Ti (CH ₃) ₂(CH ₃CH ₂) ₂), trimethylammonium ethyl titanium (Ti (CH ₃) ₃(CH ₃CH ₂)), triisobutyl methyltitanium (Ti (CH ₃) (i-C ₄H ₉) ₃), diisobutyl dimethyl-titanium (Ti (CH ₃) ₂(i-C ₄H ₉) ₂), trimethylammonium isobutyl-titanium (Ti (CH ₃) ₃(i-C ₄H ₉)), triisobutyl ethyl titanium (Ti (CH ₃CH ₂) (i-C ₄H ₉) ₃), diisobutyl diethylammonium titanium (Ti (CH ₃CH ₂) ₂(i-C ₄H ₉) ₂), triethyl isobutyl-titanium (Ti (CH ₃CH ₂) ₃(i-C ₄H ₉)), three normal-butyl methyltitanium (Ti (CH ₃) (C ₄H ₉) ₃), di-n-butyl dimethyl-titanium (Ti (CH ₃) ₂(C ₄H ₉) ₂), trimethylammonium normal-butyl titanium (Ti (CH ₃) ₃(C ₄H ₉)), three normal-butyl methyltitanium (Ti (CH ₃CH ₂) (C ₄H ₉) ₃), di-n-butyl diethylammonium titanium (Ti (CH ₃CH ₂) ₂(C ₄H ₉) ₂), triethyl normal-butyl titanium (Ti (CH ₃CH ₂) ₃(C ₄H ₉)) etc.;

Tetramethyl-zirconium (Zr (CH ₃) ₄), tetraethyl-zirconium (Zr (CH ₃CH ₂) ₄), four isobutyl-zirconium (Zr (i-C ₄H ₉) ₄), tetra-n-butyl zirconium (Zr (C ₄H ₉) ₄), triethyl methylcyclopentadienyl zirconium (Zr (CH ₃) (CH ₃CH ₂) ₃), diethyl-dimethyl zirconium (Zr (CH ₃) ₂(CH ₃CH ₂) ₂), trimethylammonium ethyl zirconium (Zr (CH ₃) ₃(CH ₃CH ₂)), triisobutyl methylcyclopentadienyl zirconium (Zr (CH ₃) (i-C ₄H ₉) ₃), diisobutyl zirconium dimethyl (Zr (CH ₃) ₂(i-C ₄H ₉) ₂), trimethylammonium isobutyl-zirconium (Zr (CH ₃) ₃(i-C ₄H ₉)), triisobutyl ethyl zirconium (Zr (CH ₃CH ₂) (i-C ₄H ₉) ₃), diisobutyl diethylammonium zirconium (Zr (CH ₃CH ₂) ₂(i-C ₄H ₉) ₂), triethyl isobutyl-zirconium (Zr (CH ₃CH ₂) ₃(i-C ₄H ₉)), three normal-butyl methylcyclopentadienyl zirconium (Zr (CH ₃) (C ₄H ₉) ₃), di-n-butyl zirconium dimethyl (Zr (CH ₃) ₂(C ₄H ₉) ₂), trimethylammonium normal-butyl zirconium (Zr (CH ₃) ₃(C ₄H ₉)), three normal-butyl methylcyclopentadienyl zirconium (Zr (CH ₃CH ₂) (C ₄H ₉) ₃), di-n-butyl diethylammonium zirconium (Zr (CH ₃CH ₂) ₂(C ₄H ₉) ₂), triethyl normal-butyl zirconium (Zr (CH ₃CH ₂) ₃(C ₄H ₉)) etc.;

Tetramethyl-hafnium (Hf (CH ₃) ₄), tetraethyl-hafnium (Hf (CH ₃CH ₂) ₄), four isobutyl-hafnium (Hf (i-C ₄H ₉) ₄), tetra-n-butyl hafnium (Hf (C ₄H ₉) ₄), triethyl methylcyclopentadienyl hafnium (Hf (CH ₃) (CH ₃CH ₂) ₃), diethyl-dimethyl hafnium (Hf (CH ₃) ₂(CH ₃CH ₂) ₂), trimethylammonium ethyl hafnium (Hf (CH ₃) ₃(CH ₃CH ₂)), triisobutyl methylcyclopentadienyl hafnium (Hf (CH ₃) (i-C ₄H ₉) ₃), diisobutyl dimethyl-hafnium (Hf (CH ₃) ₂(i-C ₄H ₉) ₂), trimethylammonium isobutyl-hafnium (Hf (CH ₃) ₃(i-C ₄H ₉)), triisobutyl ethyl hafnium (Hf (CH ₃CH ₂) (i-C ₄H ₉) ₃), diisobutyl diethylammonium hafnium (Hf (CH ₃CH ₂) ₂(i-C ₄H ₉) ₂), triethyl isobutyl-hafnium (Hf (CH ₃CH ₂) ₃(i-C ₄H ₉)), three normal-butyl methylcyclopentadienyl hafnium (Hf (CH ₃) (C ₄H ₉) ₃), di-n-butyl dimethyl-hafnium (Hf (CH ₃) ₂(C ₄H ₉) ₂), trimethylammonium normal-butyl hafnium (Hf (CH ₃) ₃(C ₄H ₉)), three normal-butyl methylcyclopentadienyl hafnium (Hf (CH ₃CH ₂) (C ₄H ₉) ₃), di-n-butyl diethylammonium hafnium (Hf (CH ₃CH ₂) ₂(C ₄H ₉) ₂), triethyl normal-butyl hafnium (Hf (CH ₃CH ₂) ₃(C ₄H ₉)) etc.

As said IV B family metal alkoxide compound, such as enumerating tetramethoxy titanium (Ti (OCH ₃) ₄), purity titanium tetraethoxide (Ti (OCH ₃CH ₂) ₄), four isobutoxy titanium (Ti (i-OC ₄H ₉) ₄), four titanium n-butoxide (Ti (OC ₄H ₉) ₄), triethoxy methoxyl group titanium (Ti (OCH ₃) (OCH ₃CH ₂) ₃), diethoxy dimethoxy titanium (Ti (OCH ₃) ₂(OCH ₃CH ₂) ₂), trimethoxy ethanolato-titanium (Ti (OCH ₃) ₃(OCH ₃CH ₂)), three isobutoxy methoxyl group titanium (Ti (OCH ₃) (i-OC ₄H ₉) ₃), two isobutoxy dimethoxy titanium (Ti (OCH ₃) ₂(i-OC ₄H ₉) ₂), trimethoxy isobutoxy titanium (Ti (OCH ₃) ₃(i-OC ₄H ₉)), three isobutoxy ethanolato-titanium (Ti (OCH ₃CH ₂) (i-OC ₄H ₉) ₃), two isobutoxy diethoxy titanium (Ti (OCH ₃CH ₂) ₂(i-OC ₄H ₉) ₂), triethoxy isobutoxy titanium (Ti (OCH ₃CH ₂) ₃(i-OC ₄H ₉)), three n-butoxy methoxyl group titanium (Ti (OCH ₃) (OC ₄H ₉) ₃), two n-butoxy dimethoxy titanium (Ti (OCH ₃) ₂(OC ₄H ₉) ₂), trimethoxy titanium n-butoxide (Ti (OCH ₃) ₃(OC ₄H ₉)), three n-butoxy methoxyl group titanium (Ti (OCH ₃CH ₂) (OC ₄H ₉) ₃), two n-butoxy diethoxy titanium (Ti (OCH ₃CH ₂) ₂(OC ₄H ₉) ₂), triethoxy titanium n-butoxide (Ti (OCH ₃CH ₂) ₃(OC ₄H ₉)) etc.;

Tetramethoxy zirconium (Zr (OCH ₃) ₄), tetraethoxy zirconium (Zr (OCH ₃CH ₂) ₄), four isobutoxy zirconium (Zr (i-OC ₄H ₉) ₄), four n-butoxy zirconium (Zr (OC ₄H ₉) ₄), triethoxy methoxyl group zirconium (Zr (OCH ₃) (OCH ₃CH ₂) ₃), diethoxy dimethoxy zirconium (Zr (OCH ₃) ₂(OCH ₃CH ₂) ₂), trimethoxy oxyethyl group zirconium (Zr (OCH ₃) ₃(OCH ₃CH ₂)), three isobutoxy methoxyl group zirconium (Zr (OCH ₃) (i-OC ₄H ₉) ₃), two isobutoxy dimethoxy zirconium (Zr (OCH ₃) ₂(i-OC ₄H ₉) ₂), trimethoxy isobutoxy zirconium (Zr (OCH ₃) ₃(i-C ₄H ₉)), three isobutoxy oxyethyl group zirconium (Zr (OCH ₃CH ₂) (i-OC ₄H ₉) ₃), two isobutoxy diethoxy zirconium (Zr (OCH ₃CH ₂) ₂(i-OC ₄H ₉) ₂), triethoxy isobutoxy zirconium (Zr (OCH ₃CH ₂) ₃(i-OC ₄H ₉)), three n-butoxy methoxyl group zirconium (Zr (OCH ₃) (OC ₄H ₉) ₃), two n-butoxy dimethoxy zirconium (Zr (OCH ₃) ₂(OC ₄H ₉) ₂), trimethoxy n-butoxy zirconium (Zr (OCH ₃) ₃(OC ₄H ₉)), three n-butoxy methoxyl group zirconium (Zr (OCH ₃CH ₂) (OC ₄H ₉) ₃), two n-butoxy diethoxy zirconium (Zr (OCH ₃CH ₂) ₂(OC ₄H ₉) ₂), triethoxy n-butoxy zirconium (Zr (OCH ₃CH ₂) ₃(OC ₄H ₉)) etc.;

Tetramethoxy hafnium (Hf (OCH ₃) ₄), tetraethoxy hafnium (Hf (OCH ₃CH ₂) ₄), four isobutoxy hafnium (Hf (i-OC ₄H ₉) ₄), four n-butoxy hafnium (Hf (OC ₄H ₉) ₄), triethoxy methoxyl group hafnium (Hf (OCH ₃) (OCH ₃CH ₂) ₃), diethoxy dimethoxy hafnium (Hf (OCH ₃) ₂(OCH ₃CH ₂) ₂), trimethoxy oxyethyl group hafnium (Hf (OCH ₃) ₃(OCH ₃CH ₂)), three isobutoxy methoxyl group hafnium (Hf (OCH ₃) (i-OC ₄H ₉) ₃), two isobutoxy dimethoxy hafnium (Hf (OCH ₃) ₂(i-OC ₄H ₉) ₂), trimethoxy isobutoxy hafnium (Hf (OCH ₃) ₃(i-OC ₄H ₉)), three isobutoxy oxyethyl group hafnium (Hf (OCH ₃CH ₂) (i-OC ₄H ₉) ₃), two isobutoxy diethoxy hafnium (Hf (OCH ₃CH ₂) ₂(i-OC ₄H ₉) ₂), triethoxy isobutoxy hafnium (Hf (OCH ₃CH ₂) ₃(i-C ₄H ₉)), three n-butoxy methoxyl group hafnium (Hf (OCH ₃) (OC ₄H ₉) ₃), two n-butoxy dimethoxy hafnium (Hf (OCH ₃) ₂(OC ₄H ₉) ₂), trimethoxy n-butoxy hafnium (Hf (OCH ₃) ₃(OC ₄H ₉)), three n-butoxy methoxyl group hafnium (Hf (OCH ₃CH ₂) (OC ₄H ₉) ₃), two n-butoxy diethoxy hafnium (Hf (OCH ₃CH ₂) ₂(OC ₄H ₉) ₂), triethoxy n-butoxy hafnium (Hf (OCH ₃CH ₂) ₃(OC ₄H ₉)) etc.

As said IV B family metal alkyl halides, such as enumerating trimethylammonium titanium chloride (TiCl (CH ₃) ₃), triethyl titanium chloride (TiCl (CH ₃CH ₂) ₃), triisobutyl titanium chloride (TiCl (i-C ₄H ₉) ₃), three normal-butyl chlorination titanium (TiCl (C ₄H ₉) ₃), dimethyl-titanium dichloride (TiCl ₂(CH ₃) ₂), diethylammonium titanium dichloride (TiCl ₂(CH ₃CH ₂) ₂), diisobutyl titanium dichloride (TiCl ₂(i-C ₄H ₉) ₂), three normal-butyl chlorination titanium (TiCl (C ₄H ₉) ₃), methyl titanous chloride (Ti (CH ₃) Cl ₃), ethyl titanous chloride (Ti (CH ₃CH ₂) Cl ₃), isobutyl-titanous chloride (Ti (i-C ₄H ₉) Cl ₃), normal-butyl titanous chloride (Ti (C ₄H ₉) Cl ₃);

Trimethylammonium titanium bromide (TiBr (CH ₃) ₃), triethyl titanium bromide (TiBr (CH ₃CH ₂) ₃), triisobutyl titanium bromide (TiBr (i-C ₄H ₉) ₃), three normal-butyl bromination titanium (TiBr (C ₄H ₉) ₃), dimethyl-dibrominated titanium (TiBr ₂(CH ₃) ₂), diethylammonium dibrominated titanium (TiBr ₂(CH ₃CH ₂) ₂), diisobutyl dibrominated titanium (TiBr ₂(i-C ₄H ₉) ₂), three normal-butyl bromination titanium (TiBr (C ₄H ₉) ₃), methyl titanium tribromide (Ti (CH ₃) Br ₃), ethyl titanium tribromide (Ti (CH ₃CH ₂) Br ₃), isobutyl-titanium tribromide (Ti (i-C ₄H ₉) Br ₃), normal-butyl titanium tribromide (Ti (C ₄H ₉) Br ₃);

Trimethylammonium zirconium chloride (ZrCl (CH ₃) ₃), triethyl zirconium chloride (ZrCl (CH ₃CH ₂) ₃), triisobutyl zirconium chloride (ZrCl (i-C ₄H ₉) ₃), three normal-butyl chlorination zirconium (ZrCl (C ₄H ₉) ₃), dimethyl-zirconium dichloride (ZrCl ₂(CH ₃) ₂), diethylammonium zirconium dichloride (ZrCl ₂(CH ₃CH ₂) ₂), diisobutyl zirconium dichloride (ZrCl ₂(i-C ₄H ₉) ₂), three normal-butyl chlorination zirconium (ZrCl (C ₄H ₉) ₃), methyl tri-chlorination zirconium (Zr (CH ₃) Cl ₃), ethyl tri-chlorination zirconium (Zr (CH ₃CH ₂) Cl ₃), isobutyl-tri-chlorination zirconium (Zr (i-C ₄H ₉) Cl ₃), normal-butyl tri-chlorination zirconium (Zr (C ₄H ₉) Cl ₃);

Trimethylammonium zirconium bromide (ZrBr (CH ₃) ₃), triethyl zirconium bromide (ZrBr (CH ₃CH ₂) ₃), triisobutyl zirconium bromide (ZrBr (i-C ₄H ₉) ₃), three normal-butyl bromination zirconium (ZrBr (C ₄H ₉) ₃), dimethyl-dibrominated zirconium (ZrBr ₂(CH ₃) ₂), diethylammonium dibrominated zirconium (ZrBr ₂(CH ₃CH ₂) ₂), diisobutyl dibrominated zirconium (ZrBr ₂(i-C ₄H ₉) ₂), three normal-butyl bromination zirconium (ZrBr (C ₄H ₉) ₃), methyl tribromide zirconium (Zr (CH ₃) Br ₃), ethyl tribromide zirconium (Zr (CH ₃CH ₂) Br ₃), isobutyl-tribromide zirconium (Zr (i-C ₄H ₉) Br ₃), normal-butyl tribromide zirconium (Zr (C ₄H ₉) Br ₃);

Trimethylammonium hafnium chloride (HfCl (CH ₃) ₃), triethyl hafnium chloride (HfCl (CH ₃CH ₂) ₃), triisobutyl hafnium chloride (HfCl (i-C ₄H ₉) ₃), three normal-butyl chlorination hafnium (HfCl (C ₄H ₉) ₃), dimethyl-hafnium dichloride (HfCl ₂(CH ₃) ₂), diethylammonium hafnium dichloride (HfCl ₂(CH ₃CH ₂) ₂), diisobutyl hafnium dichloride (HfCl ₂(i-C ₄H ₉) ₂), three normal-butyl chlorination hafnium (HfCl (C ₄H ₉) ₃), methyl tri-chlorination hafnium (Hf (CH ₃) Cl ₃), ethyl tri-chlorination hafnium (Hf (CH ₃CH ₂) Cl ₃), isobutyl-tri-chlorination hafnium (Hf (i-C ₄H ₉) Cl ₃), normal-butyl tri-chlorination hafnium (Hf (C ₄H ₉) Cl ₃);

Trimethylammonium bromination hafnium (HfBr (CH ₃) ₃), triethyl bromination hafnium (HfBr (CH ₃CH ₂) ₃), triisobutyl bromination hafnium (HfBr (i-C ₄H ₉) ₃), three normal-butyl bromination hafnium (HfBr (C ₄H ₉) ₃), dimethyl-dibrominated hafnium (HfBr ₂(CH ₃) ₂), diethylammonium dibrominated hafnium (HfBr ₂(CH ₃CH ₂) ₂), diisobutyl dibrominated hafnium (HfBr ₂(i-C ₄H ₉) ₂), three normal-butyl bromination hafnium (HfBr (C ₄H ₉) ₃), methyl tribromide hafnium (Hf (CH ₃) Br ₃), ethyl tribromide hafnium (Hf (CH ₃CH ₂) Br ₃), isobutyl-tribromide hafnium (Hf (i-C ₄H ₉) Br ₃), normal-butyl tribromide hafnium (Hf (C ₄H ₉) Br ₃).

As said IV B family metal alkoxide halogenide, such as enumerating trimethoxy titanium chloride (TiCl (OCH ₃) ₃), triethoxy titanium chloride (TiCl (OCH ₃CH ₂) ₃), three isobutoxy titanium chloride (TiCl (i-OC ₄H ₉) ₃), three n-butoxy titanium chloride (TiCl (OC ₄H ₉) ₃), dimethoxy titanium dichloride (TiCl ₂(OCH ₃) ₂), diethoxy titanium dichloride (TiCl ₂(OCH ₃CH ₂) ₂), two isobutoxy titanium dichloride (TiCl ₂(i-OC ₄H ₉) ₂), three n-butoxy titanium chloride (TiCl (OC ₄H ₉) ₃), methoxyl group titanous chloride (Ti (OCH ₃) Cl ₃), oxyethyl group titanous chloride (Ti (OCH ₃CH ₂) Cl ₃), isobutoxy titanous chloride (Ti (i-C ₄H ₉) Cl ₃), n-butoxy titanous chloride (Ti (OC ₄H ₉) Cl ₃);

Trimethoxy titanium bromide (TiBr (OCH ₃) ₃), triethoxy titanium bromide (TiBr (OCH ₃CH ₂) ₃), three isobutoxy titanium bromide (TiBr (i-OC ₄H ₉) ₃), three n-butoxy titanium bromide (TiBr (OC ₄H ₉) ₃), dimethoxy dibrominated titanium (TiBr ₂(OCH ₃) ₂), diethoxy dibrominated titanium (TiBr ₂(OCH ₃CH ₂) ₂), two isobutoxy dibrominated titanium (TiBr ₂(i-OC ₄H ₉) ₂), three n-butoxy titanium bromide (TiBr (OC ₄H ₉) ₃), methoxyl group titanium tribromide (Ti (OCH ₃) Br ₃), oxyethyl group titanium tribromide (Ti (OCH ₃CH ₂) Br ₃), isobutoxy titanium tribromide (Ti (i-C ₄H ₉) Br ₃), n-butoxy titanium tribromide (Ti (OC ₄H ₉) Br ₃);

Trimethoxy zirconium chloride (ZrCl (OCH ₃) ₃), triethoxy zirconium chloride (ZrCl (OCH ₃CH ₂) ₃), three isobutoxy zirconium chloride (ZrCl (i-OC ₄H ₉) ₃), three n-butoxy zirconium chloride (ZrCl (OC ₄H ₉) ₃), dimethoxy zirconium dichloride (ZrCl ₂(OCH ₃) ₂), diethoxy zirconium dichloride (ZrCl ₂(OCH ₃CH ₂) ₂), two isobutoxy zirconium dichloride (ZrCl ₂(i-OC ₄H ₉) ₂), three n-butoxy zirconium chloride (ZrCl (OC ₄H ₉) ₃), methoxyl group tri-chlorination zirconium (Zr (OCH ₃) Cl ₃), oxyethyl group tri-chlorination zirconium (Zr (OCH ₃CH ₂) Cl ₃), isobutoxy tri-chlorination zirconium (Zr (i-C ₄H ₉) Cl ₃), n-butoxy tri-chlorination zirconium (Zr (OC ₄H ₉) Cl ₃);

Trimethoxy zirconium bromide (ZrBr (OCH ₃) ₃), triethoxy zirconium bromide (ZrBr (OCH ₃CH ₂) ₃), three isobutoxy zirconium bromide (ZrBr (i-OC ₄H ₉) ₃), three n-butoxy zirconium bromide (ZrBr (OC ₄H ₉) ₃), dimethoxy dibrominated zirconium (ZrBr ₂(OCH ₃) ₂), diethoxy dibrominated zirconium (ZrBr ₂(OCH ₃CH ₂) ₂), two isobutoxy dibrominated zirconium (ZrBr ₂(i-OC ₄H ₉) ₂), three n-butoxy zirconium bromide (ZrBr (OC ₄H ₉) ₃), methoxyl group tribromide zirconium (Zr (OCH ₃) Br ₃), oxyethyl group tribromide zirconium (Zr (OCH ₃CH ₂) Br ₃), isobutoxy tribromide zirconium (Zr (i-C ₄H ₉) Br ₃), n-butoxy tribromide zirconium (Zr (OC ₄H ₉) Br ₃);

Trimethoxy hafnium chloride (HfCl (OCH ₃) ₃), triethoxy hafnium chloride (HfCl (OCH ₃CH ₂) ₃), three isobutoxy hafnium chloride (HfCl (i-OC ₄H ₉) ₃), three n-butoxy hafnium chloride (HfCl (OC ₄H ₉) ₃), dimethoxy hafnium dichloride (HfCl ₂(OCH ₃) ₂), diethoxy hafnium dichloride (HfCl ₂(OCH ₃CH ₂) ₂), two isobutoxy hafnium dichloride (HfCl ₂(i-OC ₄H ₉) ₂), three n-butoxy hafnium chloride (HfCl (OC ₄H ₉) ₃), methoxyl group tri-chlorination hafnium (Hf (OCH ₃) Cl ₃), oxyethyl group tri-chlorination hafnium (Hf (OCH ₃CH ₂) Cl ₃), isobutoxy tri-chlorination hafnium (Hf (i-C ₄H ₉) Cl ₃), n-butoxy tri-chlorination hafnium (Hf (OC ₄H ₉) Cl ₃);

Trimethoxy bromination hafnium (HfBr (OCH ₃) ₃), triethoxy bromination hafnium (HfBr (OCH ₃CH ₂) ₃), three isobutoxy bromination hafnium (HfBr (i-OC ₄H ₉) ₃), three n-butoxy bromination hafnium (HfBr (OC ₄H ₉) ₃), dimethoxy dibrominated hafnium (HfBr ₂(OCH ₃) ₂), diethoxy dibrominated hafnium (HfBr ₂(OCH ₃CH ₂) ₂), two isobutoxy dibrominated hafnium (HfBr ₂(i-OC ₄H ₉) ₂), three n-butoxy bromination hafnium (HfBr (OC ₄H ₉) ₃), methoxyl group tribromide hafnium (Hf (OCH ₃) Br ₃), oxyethyl group tribromide hafnium (Hf (OCH ₃CH ₂) Br ₃), isobutoxy tribromide hafnium (Hf (i-C ₄H ₉) Br ₃), n-butoxy tribromide hafnium (Hf (OC ₄H ₉) Br ₃).

As said IV B family metallic compound, preferred said IV B family metal halide, more preferably TiCl ₄, TiBr ₄, ZrCl ₄, ZrBr ₄, HfCl ₄And HfBr ₄, TiCl most preferably ₄And ZrCl ₄

These IV B family metallic compound can use a kind of separately, perhaps uses multiple with ratio combination arbitrarily.

According to the present invention, make the chemical processing agent and the said optional porous support reaction that are selected from said IV B family metallic compound through thermal activation treatment, obtain to modify carrier (below be called chemical treatment reaction I); Perhaps, make chemical processing agent that is selected from said IV B family metallic compound and the complex carrier reaction that is described below, obtain load type non-metallocene catalyst of the present invention (below be called chemical treatment reaction II).

According to the present invention, in said chemical treatment reaction I and said chemical treatment reaction II, employed separately said chemical processing agent can be the same or different.

As the mode of carrying out said chemical treatment reaction I or chemical treatment reaction II (unless otherwise indicated, following content is with being applicable to said chemical treatment reaction I and II simultaneously), such as enumerating following content.

When said chemical processing agent is liquid state at normal temperatures; Can use said chemical processing agent through the mode that in the reaction object that remains to utilize this chemical processing agent to handle (such as said optional through the porous support of thermal activation treatment or the complex carrier that is described below, as follows), directly drips the said chemical processing agent of predetermined amount.

When said chemical processing agent when being solid-state at normal temperatures, for measure with easy to operate for the purpose of, preferably use said chemical processing agent with the form of solution.Certainly, when said chemical processing agent is liquid state at normal temperatures, also can use said chemical processing agent as required sometimes, not have special qualification with the form of solution.

When the solution of the said chemical processing agent of preparation, to this moment employed solvent do not have special qualification, as long as it can dissolve this chemical processing agent.

Particularly, can enumerate C _5-12Alkane, C _5-12Naphthenic hydrocarbon, halo C _5-12Alkane, halo C _5-12Naphthenic hydrocarbon, C _6-12Aromatic hydrocarbons or halo C _6-12Aromatic hydrocarbons etc.; Such as enumerating pentane, hexane, heptane, octane, nonane, decane, undecane, dodecyl, pentamethylene, hexanaphthene, suberane, cyclooctane, toluene, ethylbenzene, YLENE, chloro-pentane, chloro-hexane, chloro heptane, chloro octane, chloro nonane, chloro decane, chloro undecane, chlorinated dodecane, chlorocyclohexane, chlorotoluene, chloro ethylbenzene and xylene monochloride etc.; Wherein preferred pentane, hexane, decane, hexanaphthene and toluene, most preferably hexane and toluene.

These solvents can use a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

It the concentration of said chemical processing agent in its solution is not had special qualification, can suitably select as required, as long as can realize implementing said chemical treatment with the said chemical processing agent of predetermined amount.As previously mentioned,, can directly use chemical processing agent to carry out said processing, but use after also can it being modulated into the chemical treatment agent solution if chemical processing agent is liquid.Be that the volumetric molar concentration of said chemical processing agent in its solution generally is set at 0.01～1.0mol/L, but is not limited to this easily.

As carrying out said chemically treated method; Such as enumerating; Under the situation that adopts solid chemical processing agent (such as zirconium tetrachloride); The solution that at first prepares said chemical processing agent, the said chemical processing agent of adding (the preferred dropping) predetermined amount in described pending reaction object (such as said optional through the porous support of thermal activation treatment or the complex carrier that is described below, as follows) then; Under the situation that adopts liquid chemical treatment agent (such as titanium tetrachloride); Can be directly (but also can after being prepared into solution) the said chemical processing agent of predetermined amount is added in (the preferred dropping) described pending reaction object; And chemical treatment reaction (in case of necessity by stirring) was carried out 0.5～24 hour; Preferred 1～8 hour, more preferably 2～6 hours, filter then, wash and dry getting final product.

Based on the present invention, said filtration, washing and drying can adopt conventional method to carry out, and wherein washer solvent can adopt used identical solvent when dissolving said chemical treatments.This washing is generally carried out 1～8 time, and preferred 2～6 times, most preferably 2～4 times.

So far, through aforesaid chemical treatment reaction I, obtained the modification carrier.

According to the present invention, magnesium compound is dissolved in the solvent (not comprising alcoholic solvent), obtain magnesium compound solution.

Below said magnesium compound is carried out bright specifically.

According to the present invention, term " magnesium compound " uses the common notion in this area, refers to as the conventional organic or inorganic solid water-free magnesium-containing compound that uses of the carrier of supported olefin polymerization catalyst.

According to the present invention, as said magnesium compound, such as enumerating magnesium halide, alkoxyl group magnesium halide, alkoxyl magnesium, alkyl magnesium, alkyl halide magnesium and alkyl alkoxy magnesium.

Particularly, as said magnesium halide, such as enumerating magnesium chloride (MgCl ₂), magnesium bromide (MgBr ₂), magnesium iodide (MgI ₂) and Sellaite (MgF ₂) etc., wherein preferred magnesium chloride.

As said alkoxyl group magnesium halide, such as enumerating methoxyl group chlorination magnesium (Mg (OCH ₃) Cl), oxyethyl group magnesium chloride (Mg (OC ₂H ₅) Cl), propoxy-magnesium chloride (Mg (OC ₃H ₇) Cl), n-butoxy magnesium chloride (Mg (OC ₄H ₉) Cl), isobutoxy magnesium chloride (Mg (i-OC ₄H ₉) Cl), methoxyl group magnesium bromide (Mg (OCH ₃) Br), oxyethyl group magnesium bromide (Mg (OC ₂H ₅) Br), propoxy-magnesium bromide (Mg (OC ₃H ₇) Br), n-butoxy magnesium bromide (Mg (OC ₄H ₉) Br), isobutoxy magnesium bromide (Mg (i-OC ₄H ₉) Br), methoxyl group magnesium iodide (Mg (OCH ₃) I), oxyethyl group magnesium iodide (Mg (OC ₂H ₅) I), propoxy-magnesium iodide (Mg (OC ₃H ₇) I), n-butoxy magnesium iodide (Mg (OC ₄H ₉) I) and isobutoxy magnesium iodide (Mg (i-OC ₄H ₉) I) etc., wherein preferred methoxyl group chlorination magnesium, oxyethyl group magnesium chloride and isobutoxy magnesium chloride.

As said alkoxyl magnesium, such as enumerating magnesium methylate (Mg (OCH ₃) ₂), magnesium ethylate (Mg (OC ₂H ₅) ₂), propoxy-magnesium (Mg (OC ₃H ₇) ₂), butoxy magnesium (Mg (OC ₄H ₉) ₂), isobutoxy magnesium (Mg (i-OC ₄H ₉) ₂) and ₂-ethyl hexyl oxy magnesium (Mg (OCH ₂CH (C ₂H ₅) C ₄H_) ₂) etc., wherein preferred magnesium ethylate and isobutoxy magnesium.

As said alkyl magnesium, such as enumerating methyl magnesium (Mg (CH ₃) ₂), magnesium ethide (Mg (C ₂H ₅) ₂), propyl group magnesium (Mg (C ₃H ₇) ₂), normal-butyl magnesium (Mg (C ₄H ₉) ₂) and isobutyl-magnesium (Mg (i-C ₄H ₉) ₂) etc., wherein preferred magnesium ethide and normal-butyl magnesium.

As said alkyl halide magnesium, such as enumerating methylmagnesium-chloride (Mg (CH ₃) Cl), ethylmagnesium chloride (Mg (C ₂H ₅) Cl), propyl group magnesium chloride (Mg (C ₃H ₇) Cl), normal-butyl chlorination magnesium (Mg (C ₄H ₉) Cl), isobutyl-chlorination magnesium (Mg (i-C ₄H ₉) Cl), methyl-magnesium-bromide (Mg (CH ₃) Br), ethylmagnesium bromide (Mg (C ₂H ₅) Br), propyl group magnesium bromide (Mg (C ₃H ₇) Br), normal-butyl bromination magnesium (Mg (C ₄H ₉) Br), isobutyl-bromination magnesium (Mg (i-C ₄H ₉) Br), methyl magnesium iodide (Mg (CH ₃) I), ethyl magnesium iodide (Mg (C ₂H ₅) I), propyl group magnesium iodide (Mg (C ₃H ₇) I), normal-butyl iodate magnesium (Mg (C ₄H ₉) I) and isobutyl-iodate magnesium (Mg (i-C ₄H ₉) I) etc., wherein preferable methyl magnesium chloride, ethylmagnesium chloride and isobutyl-chlorination magnesium.

As said alkyl alkoxy magnesium, such as enumerating methyl methoxy base magnesium (Mg (OCH ₃) (CH ₃)), methyl ethoxy magnesium (Mg (OC ₂H ₅) (CH ₃)), methyl propoxy-magnesium (Mg (OC ₃H ₇) (CH ₃)), methyl n-butoxy magnesium (Mg (OC ₄H ₉) (CH ₃)), methyl isobutoxy magnesium (Mg (i-OC ₄H ₉) (CH ₃)), ethyl magnesium methylate (Mg (OCH ₃) (C ₂H ₅)), ethyl magnesium ethylate (Mg (OC ₂H ₅) (C ₂H ₅)), ethyl propoxy-magnesium (Mg (OC ₃H ₇) (C ₂H ₅)), ethyl n-butoxy magnesium (Mg (OC ₄H ₉) (C ₂H ₅)), ethyl isobutoxy magnesium (Mg (i-OC ₄H ₉) (C ₂H ₅)), propyl group magnesium methylate (Mg (OCH ₃) (C ₃H ₇)), propyl group magnesium ethylate (Mg (OC ₂H ₅) (C ₃H ₇)), propyl group propoxy-magnesium (Mg (OC ₃H ₇) (C ₃H ₇)), propyl group n-butoxy magnesium (Mg (OC ₄H ₉) (C ₃H ₇)), propyl group isobutoxy magnesium (Mg (i-OC ₄H ₉) (C ₃H ₇)), normal-butyl magnesium methylate (Mg (OCH ₃) (C ₄H ₉)), normal-butyl magnesium ethylate (Mg (OC ₂H ₅) (C ₄H ₉)), normal-butyl propoxy-magnesium (Mg (OC ₃H ₇) (C ₄H ₉)), normal-butyl n-butoxy magnesium (Mg (OC ₄H ₉) (C ₄H ₉)), normal-butyl isobutoxy magnesium (Mg (i-OC ₄H ₉) (C ₄H ₉)), isobutyl-magnesium methylate (Mg (OCH ₃) (i-C ₄H ₉)), isobutyl-magnesium ethylate (Mg (OC ₂H ₅) (i-C ₄H ₉)), isobutyl-propoxy-magnesium (Mg (OC ₃H ₇) (i-C ₄H ₉)), isobutyl-n-butoxy magnesium (Mg (OC ₄H ₉) (i-C ₄H ₉)) and isobutyl-isobutoxy magnesium (Mg (i-OC ₄H ₉) (i-C ₄H ₉)) etc., wherein preferred butyl magnesium ethylate.

These magnesium compounds can use a kind of separately, also can multiple mixing use, and do not have special restriction.

When using with multiple blended form, the mol ratio between any two kinds of magnesium compounds in the said magnesium compound mixture is such as being 0.25～4: 1, preferred 0.5～3: 1, more preferably 1～2: 1.

Below carry out bright specifically to the step that obtains said magnesium compound solution.

Particularly, make said magnesium compound (solid) be dissolved in appropriate solvent (promptly being used for dissolving the solvent of said magnesium compound), thereby obtain said magnesium compound solution.

As said solvent, such as enumerating C _6-12Aromatic hydrocarbon, halo C _6-12Aromatic hydrocarbon, ester and ether equal solvent.Specifically such as enumerating toluene, YLENE, trimethylbenzene, ethylbenzene, diethylbenzene, chlorotoluene, chloro ethylbenzene, bromo toluene, bromo ethylbenzene, ETHYLE ACETATE and THF etc.Wherein, preferred C _6-12Aromatic hydrocarbon and THF, most preferably THF.

According to the present invention one preferred embodiment, said solvent preferably can dissolve said magnesium compound (solid) and Nonmetallocene title complex hereinafter described simultaneously.At this moment, as said solvent, such as enumerating said C _6-12Aromatic hydrocarbon, said halo C _6-12Aromatic hydrocarbon and THF etc.

It is pointed out that the present invention in preparation during said load type non-metallocene catalyst, in any step, all do not use alcoholic solvent (such as aromatic alcohols such as fatty alcohols such as ethanol, phenylcarbinols etc.) as solvent.

These solvents can use a kind of separately, also can use with the multiple mixing of ratio arbitrarily.

In order to prepare said magnesium compound solution, said magnesium compound (perhaps according to circumstances, with said magnesium compound and said Nonmetallocene title complex) metering added to dissolve in the said solvent to getting final product.When the said magnesium compound solution of preparation; Ratio in the said magnesium compound (solid) of magnesium elements and the said solvent that is used to dissolve said magnesium compound is generally 1mol: 75～400ml; Preferred 1mol: 150～300ml, more preferably 1mol: 200～250ml.

Preparation time (being the dissolution time of said magnesium compound etc.) to said magnesium compound solution does not have special qualification, but is generally 0.5～24h, preferred 4～24h.In this preparation process, can utilize and stir the dissolving promote said magnesium compound etc.This stirring can be adopted any form, such as stirring rake (rotating speed is generally 10～1000 rev/mins) etc.As required, can promote dissolving through suitable heating (but top temperature must be lower than the boiling point of said solvent) sometimes.

According to the present invention; Term " Nonmetallocene title complex " refers to a kind of active organometallics of olefinic polymerization catalysis (therefore said Nonmetallocene title complex also is called as non-metallocene olefin polymerization property title complex sometimes) that when making up with aikyiaiurnirsoxan beta, can demonstrate; This compound comprises central metal atom and at least one and said central metal atom with co-ordination bond bonded polydentate ligand (preferably tridentate ligand or more polydentate ligand), and term " Nonmetallocene part " is aforesaid polydentate ligand.

According to the present invention, said Nonmetallocene title complex is selected from the compound with following chemical structural formula:

According to this chemical structural formula, the part that forms co-ordination bond with central metal atom M comprises n radicals X and m polydentate ligand (structural formula in the bracket).According to the chemical structural formula of said polydentate ligand, group A, D and E (group is used in coordination) form co-ordination bond with atom (such as heteroatomss such as N, O, S, Se and P) with said central metal atom M through the contained coordination of these groups.

According to the present invention, all parts (comprising said radicals X and said polydentate ligand) with negative charge sum absolute value and said central metal atom M positively charged absolute value identical.

In a more concrete embodiment, said Nonmetallocene title complex is selected from compound (A) and the compound (B) with following chemical structural formula.

In a more concrete embodiment, said Nonmetallocene title complex is selected from compound (A-1) to compound (A-4) with following chemical structural formula and compound (B-1) to compound (B-4).

In above all chemical structural formulas,

Q is 0 or 1;

D is 0 or 1;

M is 1,2 or 3;

M is selected from periodic table of elements III-th family to XI family atoms metal, and preferred IVB family atoms metal is such as enumerating Ti (IV), Zr (IV), Hf (IV), Cr (III), Fe (III), Ni (II), Pd (II) or Co (II);

N is 1,2,3 or 4, depends on the valence state of said central metal atom M;

X is selected from halogen, Wasserstoffatoms, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, nitrogen-containing group, sulfur-containing group, boron-containing group, contain aluminium base group, phosphorus-containing groups, silicon-containing group, germanic group or contain tin group, a plurality of X can be identical, also can be different, can also become key or Cheng Huan each other;

A be selected from Sauerstoffatom, sulphur atom, selenium atom, -NR ²³R ²⁴,-N (O) R ²⁵R ²⁶,

-PR ²⁸R ²⁹,-P (O) R ³⁰OR ³¹, sulfuryl, sulfoxide group or-Se (O) R ³⁹, wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

B is selected from nitrogen-atoms, nitrogen-containing group, phosphorus-containing groups or C ₁-C ₃₀Alkyl;

D is selected from nitrogen-atoms, Sauerstoffatom, sulphur atom, selenium atom, phosphorus atom, nitrogen-containing group, phosphorus-containing groups, C ₁-C ₃₀Alkyl, sulfuryl, sulfoxide group,

-N (O) R ²⁵R ²⁶,

Or-P (O) R ³²(OR ³³), wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

E is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid that (CN), wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

F is selected from nitrogen-atoms, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

G is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Y is selected from Sauerstoffatom, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

Z is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid (CN), such as enumerating-NR ²³R ²⁴,-N (O) R ²⁵R ²⁶,-PR ²⁸R ²⁹,-P (O) R ³⁰R ³¹,-OR ³⁴,-SR ³⁵,-S (O) R ³⁶,-SeR ³⁸Or-Se (O) R ³⁹, wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

→ represent singly-bound or two key;

-represent covalent linkage or ionic linkage;

---represent co-ordination bond, covalent linkage or ionic linkage;

R ¹To R ⁴, R ⁶To R ³⁶, R ³⁸And R ³⁹Be selected from hydrogen, C independently of one another ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl (wherein preferred halo alkyl, such as-CH ₂Cl and-CH ₂CH ₂Cl) or safing function property group, above-mentioned group can be the same or different to each other, and wherein adjacent group is such as R ¹With R ², R ⁶With R ⁷, R ⁷With R ⁸, R ⁸With R ⁹, R ¹³With R ¹⁴, R ¹⁴With R ¹⁵, R ¹⁵With R ¹⁶, R ¹⁸With R ¹⁹, R ¹⁹With R ²⁰, R ²⁰With R ²¹, R ²³With R ²⁴, perhaps R ²⁵With R ²⁶Deng combining togather into key or Cheng Huan, be preferably formed aromatic ring, such as unsubstituted phenyl ring or by 1-4 C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl (wherein preferred halo alkyl, such as-CH ₂Cl and-CH ₂CH ₂Cl) or the substituted phenyl ring of safing function property group, and

R ⁵Be selected from lone-pair electron on the nitrogen, hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, sulfur-containing group, nitrogen-containing group, contain seleno group or phosphorus-containing groups; Work as R ⁵For oxy radical, sulfur-containing group, nitrogen-containing group, when containing seleno group or phosphorus-containing groups, R ⁵In N, O, S, P and Se can be used as coordination and carry out coordination with atom and said center IV B family atoms metal.

According to the present invention, in aforementioned all chemical structural formulas, as the case may be, any adjacent two or more groups are such as R ²¹With group Z, perhaps R ¹³With group Y, can combine togather into ring, be preferably formed and comprise the heteroatomic C that comes from said group Z or Y ₆-C ₃₀Heteroaromatic, such as pyridine ring etc., wherein said heteroaromatic is optional to be selected from C by one or more ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀The substituting group of alkyl and safing function property group replaces.

In context of the present invention,

Said halogen is selected from F, Cl, Br or I;

Said nitrogen-containing group is selected from

-NR ²³R ²⁴,-T-NR ²³R ²⁴Or-N (O) R ²⁵R ²⁶

Said phosphorus-containing groups is selected from

-PR ²⁸R ²⁹,-P (O) R ³⁰R ³¹Or-P (O) R ³²(OR ³³);

Said oxy radical be selected from hydroxyl ,-OR ³⁴With-T-OR ³⁴

Said sulfur-containing group is selected from-SR ³⁵,-T-SR ³⁵,-S (O) R ³⁶Or-T-SO ₂R ³⁷

The said seleno group that contains is selected from-SeR ³⁸,-T-SeR ³⁸,-Se (O) R ³⁹Or-T-Se (O) R ³⁹

Said group T is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group; With

Said R ³⁷Be selected from hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group.

In context of the present invention, said C ₁-C ₃₀Alkyl is selected from C ₁-C ₃₀Alkyl (preferred C ₁-C ₆Alkyl is such as isobutyl-), C ₇-C ₅₀Alkaryl (such as tolyl, xylyl, diisobutyl phenyl etc.), C ₇-C ₅₀Aralkyl (such as benzyl), C ₃-C ₃₀Cyclic alkyl, C ₂-C ₃₀Thiazolinyl, C ₂-C ₃₀Alkynyl, C ₆-C ₃₀Aryl (such as phenyl, naphthyl, anthryl etc.), C ₈-C ₃₀Condensed ring radical or C ₄-C ₃₀Heterocyclic radical, wherein said heterocyclic radical contain 1-3 heteroatoms that is selected from nitrogen-atoms, Sauerstoffatom or sulphur atom, such as pyridyl, pyrryl, furyl or thienyl etc.

According to the present invention, in context of the present invention, according to the particular case of the relevant group of its bonded, said C ₁-C ₃₀Alkyl refers to C sometimes ₁-C ₃₀(divalent group perhaps is called C to hydrocarbon two bases ₁-C ₃₀Alkylene) or C ₁-C ₃₀Hydrocarbon three bases (trivalent group), this is obvious to those skilled in the art.

In context of the present invention, said substituted C ₁-C ₃₀Alkyl refers to the aforementioned C that has one or more inert substituents ₁-C ₃₀Alkyl.So-called inert substituent refers to these substituting groups aforementioned coordination (is referred to aforementioned group A, D, E, F, Y and Z, the perhaps also optional radicals R that comprises with group ⁵) there is not substantial interference with the coordination process of said central metal atom M; In other words, limit by the chemical structure of polydentate ligand according to the invention, these substituting groups do not have ability or have no chance (such as the influence that receives steric hindrance etc.) coordination reaction takes place and form co-ordination bond with said central metal atom M.Generally speaking, said inert substituent refers to aforementioned halogen or C ₁-C ₃₀Alkyl (preferred C ₁-C ₆Alkyl is such as isobutyl-).

In context of the present invention, said safing function property group does not comprise aforesaid C ₁-C ₃₀Alkyl and aforesaid substituted C ₁-C ₃₀Alkyl.As said safing function property group, such as enumerating aforementioned halogen, aforementioned oxy radical, aforementioned nitrogen-containing group, silicon-containing group, germanic group, aforementioned sulfur-containing group, containing tin group, C ₁-C ₁₀Ester group or nitro (NO ₂) etc.

In context of the present invention, limit by the chemical structure of polydentate ligand according to the invention, said safing function property group has following characteristics:

(1) do not disturb said group A, D, E, F, Y or Z and said central metal atom M the coordination process and

(2) coordination ability with said central metal atom M is lower than said A, D, E, F, Y and Z group, and does not replace the existing coordination of these groups and said central metal atom M.

In context of the present invention, said boron-containing group is selected from BF ₄ ^-, (C ₆F ₅) ₄B ^-Or (R ⁴⁰BAr ₃) ^-Saidly contain aluminium base group and be selected from aluminum alkyls, AlPh ₄ ^-, AlF ₄ ^-, AlCl ₄ ^-, AlBr ₄ ^-, AlI ₄ ^-Or R ⁴¹AlAr ₃ ^-Said silicon-containing group is selected from-SiR ⁴²R ⁴³R ⁴⁴Or-T-SiR ⁴⁵Said germanic group is selected from-GeR ⁴⁶R ⁴⁷R ⁴⁸Or-T-GeR ⁴⁹Saidly contain tin group and be selected from-SnR ⁵⁰R ⁵¹R ⁵²,-T-SnR ⁵³Or-T-Sn (O) R ⁵⁴, said Ar represents C ₆-C ₃₀Aryl, and R ⁴⁰To R ⁵⁴Be selected from hydrogen, aforesaid C independently of one another ₁-C ₃₀Alkyl, aforesaid substituted C ₁-C ₃₀Alkyl or aforesaid safing function property group, above-mentioned group can be the same or different to each other, and wherein adjacent group can combine togather into key or Cheng Huan, and the definition of said group T is the same.

As said Nonmetallocene title complex, such as enumerating following compound:

Said Nonmetallocene title complex is preferably selected from following compound:

Said Nonmetallocene title complex further is preferably selected from following compound:

Said Nonmetallocene title complex more preferably is selected from following compound:

These Nonmetallocene complexs can use a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

According to the present invention, the said polydentate ligand in the said Nonmetallocene title complex is not as the normally used diether compounds of electronic donor compound capable in this area.

Said Nonmetallocene title complex or said polydentate ligand can be made according to any method well known by persons skilled in the art.About the particular content of its method of manufacture, such as can be referring to WO03/010207 and Chinese patent ZL01126323.7 and ZL02110844.7 etc., the full text that this specification sheets is introduced these documents at this point as a reference.

According to the present invention, said modification carrier, said magnesium compound solution are contacted with said Nonmetallocene title complex, obtain mixed serum.

When making said mixed serum; The way of contact of said modification carrier, said magnesium compound solution and said Nonmetallocene title complex and engagement sequence etc. there is not special qualification; Such as enumerating said modification carrier is mixed earlier with said magnesium compound solution, and then to the scheme that wherein adds said Nonmetallocene title complex; Make said modification carrier, said magnesium compound solution and said Nonmetallocene title complex blended scheme simultaneously; Said Nonmetallocene title complex and said magnesium compound are dissolved in the foregoing solvent simultaneously; Make the mixing solutions (being also referred to as magnesium compound solution hereinafter sometimes) of magnesium compound and Nonmetallocene title complex thus, and then make said modification carrier and said mixing solutions blended scheme or the like.

In addition; In order to make said mixed serum; Such as can be to the temperature of the boiling point that is lower than employed any solvent at normal temperature; Make the contact reacts of said modification carrier, said magnesium compound solution and said Nonmetallocene title complex carry out 0.1～8h, preferred 0.5～4h, optimum 1～2h (in case of necessity by stirring) gets final product.

At this moment, the mixed serum that is obtained is a kind of system of pulpous state.Though unessential, in order to ensure the homogeneity of system, this mixed serum preferably carries out certain hour (2～48h, preferred 4～24h, most preferably 6～18h) airtight leaving standstill after preparation.

Through to said mixed serum convection drying, can obtain a kind of solid product of good fluidity, complex carrier promptly of the present invention.

At this moment, said convection drying can adopt ordinary method to carry out, down dry such as inert gas atmosphere, vacuum atmosphere is dry down or vacuum atmosphere under heat drying etc., heat drying under the wherein preferred vacuum atmosphere.Carry out under the temperature (being generally 30～160 ℃, preferred 60～130 ℃) that the boiling point of any solvent that said drying generally contains in than said mixed serum is low 5～15 ℃, and be generally 2～24h time of drying, but be not limited to this sometimes.

Then,, the chemical processing agent that is selected from said IVB family metallic compound is reacted with said complex carrier, obtain load type non-metallocene catalyst of the present invention thus through aforesaid chemical treatment reaction II.

In said chemical treatment reaction II; Owing to contain said magnesium compound and said Nonmetallocene title complex in the said complex carrier; So obviously, just can not select for use this moment has the solvent of stripping capacity to dissolve said chemical processing agent to said magnesium compound or said Nonmetallocene title complex, to avoid the inappropriate stripping of these materials in treating processes.

Special embodiment according to the present invention; The preparation method of load type non-metallocene catalyst of the present invention also is included in and makes before said chemical processing agent and the reaction of said complex carrier, with the step that helps the said complex carrier of chemical processing agent pre-treatment (pre-treatment step) that is selected from aikyiaiurnirsoxan beta, aluminum alkyls or its arbitrary combination.

Below to help chemical processing agent to carry out bright specifically to said.

According to the present invention, as the said chemical processing agent that helps, such as enumerating aikyiaiurnirsoxan beta and aluminum alkyls.

As said aikyiaiurnirsoxan beta, such as enumerating the line style aikyiaiurnirsoxan beta shown in the formula (I): (R) (R) Al-(Al (R)-O) _n-O-Al (R) (R), and the ring-type aikyiaiurnirsoxan beta shown in the formula (II) :-(Al (R)-O-) _N+2-.

In aforementioned formula, radicals R is same to each other or different to each other (preferably identical), is selected from C independently of one another ₁-C ₈Alkyl, preferable methyl, ethyl and isobutyl-, most preferable; N is the arbitrary integer in the 1-50 scope, the arbitrary integer in preferred 10～30 scopes.

As said aikyiaiurnirsoxan beta, preferable methyl aikyiaiurnirsoxan beta, ethyl aikyiaiurnirsoxan beta, isobutyl aluminium alkoxide and normal-butyl alumina alkane, further preferable methyl aikyiaiurnirsoxan beta and isobutyl aluminium alkoxide.

These aikyiaiurnirsoxan beta can be used a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

As said aluminum alkyls, such as enumerating the compound shown in the following general formula (III):

Al(R) ₃ (III)

Wherein, radicals R is same to each other or different to each other (preferably identical), and is selected from C independently of one another ₁-C ₈Alkyl, preferable methyl, ethyl and isobutyl-, most preferable.

Particularly, as said aluminum alkyls, such as enumerating trimethylaluminium (Al (CH ₃) ₃), triethyl aluminum (Al (CH ₃CH ₂) ₃), tri-propyl aluminum (Al (C ₃H ₇) ₃), triisobutyl aluminium (Al (i-C ₄H ₉) ₃), three n-butylaluminum (Al (C ₄H ₉) ₃), triisopentyl aluminium (Al (i-C ₅H ₁₁) ₃), three n-pentyl aluminium (Al (C ₅H ₁₁) ₃), three hexyl aluminium (Al (C ₆H ₁₃) ₃), three isohexyl aluminium (Al (i-C ₆H ₁₃) ₃), diethylmethyl aluminium (Al (CH ₃) (CH ₃CH ₂) ₂) and dimethyl ethyl aluminium (Al (CH ₃CH ₂) (CH ₃) ₂) etc., wherein preferred trimethylaluminium, triethyl aluminum, tri-propyl aluminum and triisobutyl aluminium, most preferably triethyl aluminum and triisobutyl aluminium.

These alkyl aluminums can use a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

According to the present invention, as the said chemical processing agent that helps, can only adopt said aikyiaiurnirsoxan beta, also can only adopt said aluminum alkyls, but also can adopt any mixture of said aikyiaiurnirsoxan beta and said aluminum alkyls.And, the ratio of each component in this mixture there is not special qualification, can select arbitrarily as required.

According to the present invention, the said chemical processing agent that helps generally is to use with the form of solution.When the said solution that helps chemical treatments of preparation, to this moment employed solvent there is no particular limitation, as long as it can dissolve this and help chemical treatments.

Particularly, can enumerate C _5-12Alkane, C _5-12Naphthenic hydrocarbon, halo C _5-12Alkane, halo C _5-12Naphthenic hydrocarbon, C _6-12Aromatic hydrocarbons or halo C _6-12Aromatic hydrocarbons etc.; Such as enumerating pentane, hexane, heptane, octane, nonane, decane, undecane, dodecyl, pentamethylene, hexanaphthene, suberane, cyclooctane, toluene, ethylbenzene, YLENE, chloro-pentane, chloro-hexane, chloro heptane, chloro octane, chloro nonane, chloro decane, chloro undecane, chlorinated dodecane, chlorocyclohexane, chlorotoluene, chloro ethylbenzene and xylene monochloride etc.; Wherein preferred pentane, hexane, decane, hexanaphthene and toluene, most preferably hexane and toluene.

These solvents can use a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

Equally; In said pre-treatment step; Owing to contain said magnesium compound and said Nonmetallocene title complex in the said complex carrier; So obviously, just can not select for use this moment has the solvent of stripping capacity to dissolve the said chemical processing agent that helps to said magnesium compound or said Nonmetallocene title complex, to avoid the inappropriate stripping of these materials in treating processes.

It the said concentration of chemical processing agent in its solution that helps is not had special qualification, can suitably select as required, as long as can realize carrying out said pre-treatment with the said chemical processing agent that helps of predetermined amount.

As carrying out said pretreated method; Such as enumerating, at first prepare the said solution that helps chemical processing agent, then under the temperature of-30～60 ℃ (preferred-20～30 ℃); Be metered into (the preferred dropping) said chemical treatment agent solution (the said chemical processing agent that helps that contains predetermined amount) that helps to intending with said helping in the pretreated said complex carrier of chemical processing agent; Perhaps add said complex carrier, form reaction mixture thus, make its reaction 1～8h to the said chemical treatment agent solution amount of falling into a trap that helps; Preferred 2～6h, most preferably 3～4h (in case of necessity by stirring) gets final product.Then, with the pre-treatment product that obtained through filtration, washing (1～6 time, preferred 1～3 time) and optionally drying, and from this reaction mixture, separate, perhaps, also can be and directly be used for follow-up reactions step with the form of mixed solution without this separation.At this moment, owing to contained certain amount of solvent in the said mixed solution, so the solvent load that relates in can the said subsequent reactions step of corresponding minimizing.

Through said pre-treatment step, obtain through pretreated complex carrier thus.Then, according to carrying out said chemical treatment reaction II with said chemical processing agent, just said complex carrier is replaced with the pretreated complex carrier of said process and get final product again with aforementioned identical mode.

That is,, the chemical processing agent that is selected from said IVB family metallic compound is reacted with said complex carrier or the pretreated complex carrier of said process, obtain load type non-metallocene catalyst of the present invention thus through said chemical treatment reaction II.

According to the present invention,, make that the mol ratio in the said magnesium compound (solid) of Mg element and said Nonmetallocene title complex reaches 1: 0.01-1, preferred 1: 0.04-0.4, more preferably 1: 0.08-0.2 as the consumption of said Nonmetallocene title complex.

According to the present invention, as the consumption of the said solvent that is used to dissolve said magnesium compound, make the said magnesium compound (solid) and the ratio of said solvent reach 1mol: 75～400ml, preferred 1mol: 150～300ml, more preferably 1mol: 200～250ml.

According to the present invention,, make to reach 1: 0.1-20, preferred 1: 0.5-10, more preferably 1: 1-5 in the said magnesium compound of magnesium compound solid and the mass ratio of said porous support as the consumption of said porous support.

According to the present invention; In said chemical treatment reaction I and said chemical treatment reaction II; The consumption of said chemical processing agent can be the same or different, and selects independently of one another, thereby makes and in each chemical treatment reaction, to reach 1 in the said magnesium compound (solid) of Mg element and mol ratio in the said chemical processing agent of IVB family metal (such as Ti) element independently of one another: 0.01-1; Preferred 1: 0.01-0.50, more preferably 1: 0.10-0.30.

According to the present invention,, make to reach 1: 0-1.0, preferred 1: 0-0.5, more preferably 1: 0.1-0.5 in the said magnesium compound (solid) of Mg element and the said mol ratio of chemical processing agent that helps in the Al element as the said consumption that helps chemical processing agent.

Known to those skilled in the artly be that aforementioned all method steps all preferably carries out under the condition of anhydrous anaerobic basically.Here the content that said anhydrous basically anaerobic refers to water and oxygen in the system continues less than 10ppm.And load type non-metallocene catalyst of the present invention needs pressure-fired preservation in confined conditions subsequent use after preparation usually.

In one embodiment, the invention still further relates to the load type non-metallocene catalyst of making by the preparation method of aforesaid load type non-metallocene catalyst (being also referred to as carry type non-metallocene calalyst for polymerization of olefine sometimes).

In a further embodiment, the present invention relates to a kind of alkene homopolymerization/copolymerization process, wherein with load type non-metallocene catalyst of the present invention as catalyst for olefines polymerizing, make alkene homopolymerization or copolymerization.

With regard to this alkene homopolymerization/copolymerization process involved in the present invention; Except the following content that particularly points out; Other contents of not explaining (such as polymerization with addition manner of reactor drum, alkene consumption, catalyzer and alkene etc.); Can directly be suitable for this area conventional known those, do not have special restriction, omit its explanation at this.

According to homopolymerization/copolymerization process of the present invention; With load type non-metallocene catalyst of the present invention is Primary Catalysts; To be selected from aikyiaiurnirsoxan beta, aluminum alkyls, haloalkyl aluminium, boron fluothane, boron alkyl and the boron alkyl ammonium salt one or more is promotor, makes alkene homopolymerization or copolymerization.

Primary Catalysts and the promotor adding mode in polymerization reaction system can be to add Primary Catalysts earlier; And then the adding promotor, perhaps add promotor earlier, and then add Primary Catalysts; Or add together after both contact mixing earlier, perhaps add simultaneously respectively.Primary Catalysts and promotor added respectively fashionablely both can in same reinforced pipeline, add successively, also can in the reinforced pipeline of multichannel, add successively, and both add simultaneously respectively and fashionablely should select the multichannel pipeline that feeds in raw material.For the continous way polyreaction; The adding continuously simultaneously of the reinforced pipeline of preferred multichannel, and for the intermittence type polymerization reaction, preferably both mix back adding together in same reinforced pipeline earlier; Perhaps in same reinforced pipeline, add promotor earlier, and then add Primary Catalysts.

According to the present invention; Reactive mode to said alkene homopolymerization/copolymerization process does not have special qualification; Can adopt well known in the art those, such as enumerating slurry process, emulsion method, solution method, substance law and vapor phase process etc., wherein preferred slurries method and vapor phase process.

According to the present invention, as said alkene, such as enumerating C ₂～C ₁₀Monoolefine, diolefin, cyclic olefin and other ethylenically unsaturated compounds.

Particularly, as said C ₂～C ₁₀Monoolefine is such as enumerating ethene, propylene, 1-butylene, 1-hexene, 1-heptene, 4-methyl-1-pentene, 1-octene, 1-decene, 1-hendecene, 1-laurylene and vinylbenzene etc.; As said cyclic olefin, such as enumerating 1-cyclopentenes and norbornylene etc.; As said diolefin, such as enumerating 1,4-divinyl, 2,5-pentadiene, 1,6-hexadiene, norbornadiene and 1,7-octadiene etc.; And as said other ethylenically unsaturated compounds, such as enumerating vinyl acetate and (methyl) propenoate etc.Wherein, the homopolymerization of optimal ethylene, the perhaps copolymerization of ethene and propylene, 1-butylene or 1-hexene.

According to the present invention, homopolymerization refers to only a kind of polymerization of said alkene, and copolymerization refers to the polymerization between the two or more said alkene.

According to the present invention, said promotor is selected from aikyiaiurnirsoxan beta, aluminum alkyls, haloalkyl aluminium, boron fluothane, boron alkyl and boron alkyl ammonium salt, wherein preferred aikyiaiurnirsoxan beta and aluminum alkyls.

As said aikyiaiurnirsoxan beta, such as enumerating the line style aikyiaiurnirsoxan beta shown in the formula (I-1): (R) (R) Al-(Al (R)-O) _n-O-Al (R) (R), and the ring-type aikyiaiurnirsoxan beta shown in the formula (II-1) :-(Al (R)-O-) _N+2-.

In aforementioned formula, radicals R is same to each other or different to each other (preferably identical), is selected from C independently of one another ₁-C ₈Alkyl, preferable methyl, ethyl and isobutyl-, most preferable; N is the arbitrary integer in the 1-50 scope, the arbitrary integer in preferred 10～30 scopes.

As said aikyiaiurnirsoxan beta, preferable methyl aikyiaiurnirsoxan beta, ethyl aikyiaiurnirsoxan beta, isobutyl aluminium alkoxide and normal-butyl alumina alkane, further preferable methyl aikyiaiurnirsoxan beta and isobutyl aluminium alkoxide, and most preferable aikyiaiurnirsoxan beta.

These aikyiaiurnirsoxan beta can be used a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

As said aluminum alkyls, such as enumerating the compound shown in the following general formula (III-1):

Al(R) ₃ (III-1)

Wherein, radicals R is same to each other or different to each other (preferably identical), and is selected from C independently of one another ₁-C ₈Alkyl, preferable methyl, ethyl and isobutyl-, most preferable.

Particularly, as said aluminum alkyls, such as enumerating trimethylaluminium (Al (CH ₃) ₃), triethyl aluminum (Al (CH ₃CH ₂) ₃), tri-propyl aluminum (Al (C ₃H ₇) ₃), triisobutyl aluminium (Al (i-C ₄H ₉) ₃), three n-butylaluminum (Al (C ₄H ₉) ₃), triisopentyl aluminium (Al (i-C ₅H ₁₁) ₃), three n-pentyl aluminium (Al (C ₅H ₁₁) ₃), three hexyl aluminium (Al (C ₆H ₁₃) ₃), three isohexyl aluminium (Al (i-C ₆H ₁₃) ₃), diethylmethyl aluminium (Al (CH ₃) (CH ₃CH ₂) ₂) and dimethyl ethyl aluminium (Al (CH ₃CH ₂) (CH ₃) ₂) etc., wherein preferred trimethylaluminium, triethyl aluminum, tri-propyl aluminum and triisobutyl aluminium, further preferred triethyl aluminum and triisobutyl aluminium, and triethyl aluminum most preferably.

These alkyl aluminums can use a kind of separately, perhaps are used in combination multiple with ratio arbitrarily.

As said haloalkyl aluminium, said boron fluothane, said boron alkyl and said boron alkyl ammonium salt, can directly use conventional those that use in this area, do not have special restriction.

In addition, according to the present invention, said co-catalyst can use a kind of separately, also can be as required be used in combination multiple aforesaid co-catalyst with ratio arbitrarily, does not have special restriction.

According to the present invention,, need use polymerization to use solvent sometimes according to the difference of the reactive mode of said alkene homopolymerization/copolymerization process.

Use solvent as said polymerization, can use this area conventional those that use when carrying out alkene homopolymerization/copolymerization, do not have special restriction.

Use solvent as said polymerization, such as enumerating C _4-10Alkane (such as butane, pentane, hexane, heptane, octane, nonane or decane etc.), halo C _1-10Alkane (such as methylene dichloride), aromatic hydrocarbon solvent (such as toluene and YLENE) etc.Wherein, preferably use hexane to use solvent as said polymerization.

These polymerizations can be used a kind of separately with solvent, perhaps be used in combination multiple with ratio arbitrarily.

According to the present invention, the polymerization pressure of said alkene homopolymerization/copolymerization process is generally 0.1～10MPa, preferred 0.1～4MPa, and more preferably 1～3MPa, but be not limited to this sometimes.According to the present invention, polymeric reaction temperature is generally-40 ℃～200 ℃, and preferred 10 ℃～100 ℃, more preferably 40 ℃～90 ℃, but be not limited to this sometimes.

In addition, according to the present invention, said alkene homopolymerization/copolymerization process can carry out under the condition that has hydrogen to exist, and also can under the condition that does not have hydrogen to exist, carry out.Under situation about existing, the dividing potential drop of hydrogen can be 0.01%～99% of a said polymerization pressure, and is preferred 0.01%～50%, but is not limited to this sometimes.

According to the present invention; When carrying out said alkene homopolymerization/copolymerization process; Be generally 1～1000 in the said promotor of aluminium or boron and mol ratio: 1 in the said load type non-metallocene catalyst of central metal atom M; Preferred 10～500: 1, more preferably 15～300: 1, but be not limited to this sometimes.

Embodiment

Below adopt embodiment that the present invention is described in further detail, but the present invention is not limited to these embodiment.

(unit is g/cm to polymer stacks density ³) mensuration carry out with reference to CNS GB 1636-79.

The content of IV B family metal (such as Ti) and Mg element adopts the ICP-AES method to measure in the load type non-metallocene catalyst, and the content of Nonmetallocene part adopts analyses.

The polymerization activity of catalyzer calculates according to following method: after polyreaction finishes; Polymerisate in the reaction kettle is filtered and drying; The quality of this polymerisate of weighing then representes that divided by the ratio of the quality of used load type non-metallocene catalyst (unit is kg polymkeric substance/g catalyzer or kg polymkeric substance/gCat) for the polymerization activity of this catalyzer with this polymerisate quality.

Molecular weight Mw, Mn and the MWD (Mw/Mn) of polymkeric substance adopts the GPC V2000 type gel chromatography analyser of U.S. WATERS company to measure, and with 1,2, the 4-trichlorobenzene is a solvent, and surveying periodic temperature is 150 ℃.

Embodiment 1

Porous support adopts silicon-dioxide, i.e. silica gel, and model is the ES757 of Ineos company, at first with silica gel lasting roasting 4h and thermal activation under 600 ℃, nitrogen atmosphere.

Chemical processing agent adopts titanium tetrachloride (TiCl ₄).Take by weighing the silica gel after the 5g thermal activation, add the 60ml hexane, under the stirring at normal temperature condition, add titanium tetrachloride,, filter at 60 ℃ down behind the reaction 2h, hexane wash 3 times, each 60ml, last vacuum is drained and is obtained modifying carrier.

Magnesium compound adopts Magnesium Chloride Anhydrous, and the solvent of dissolved magnesium compound and Nonmetallocene title complex adopts THF.It is the compound of

that the Nonmetallocene title complex adopts structure.

Take by weighing Magnesium Chloride Anhydrous and Nonmetallocene title complex, add behind the tetrahydrofuran solvent under the normal temperature fully that dissolving obtains magnesium compound solution, add then and modify carrier; Stir after 2 hours; With the mixed serum even heating to 90 that is obtained ℃, directly vacuumize drying then, obtain complex carrier.

Then in this complex carrier, add the 60ml hexane, under agitation condition with 30 minutes dropping titanium tetrachlorides, 60 ℃ of following stirring reactions 4 hours; Filter; Hexane wash 2 times, each hexane consumption 60ml, vacuum-drying obtains load type non-metallocene catalyst under the normal temperature.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 2; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.08, with the solvents tetrahydrofurane proportioning be 1mol: 240ml, be 1: 0.20 with twice chemical processing agent mol ratio.

Load type non-metallocene catalyst is designated as CAT-1.

Embodiment 1-1

Basic identical with embodiment 1, but following change is arranged:

Porous support is changed into 955 of Grace company, lasting roasting 8h under 400 ℃, nitrogen atmosphere and thermal activation.Chemical processing agent changes zirconium tetrachloride (ZrCl into ₄), hexane changes toluene into.

The Nonmetallocene title complex adopts the solvent of

dissolved magnesium compound and Nonmetallocene title complex to change into toluene; And with the mixed serum even heating to 100 that is obtained ℃; Directly vacuumize drying then, obtain complex carrier.

Then in this complex carrier, add 60ml toluene, under agitation condition with 30 minutes dropping zirconium tetrachlorides, 80 ℃ of following stirring reactions 4 hours; Filter; Toluene wash 2 times, each toluene consumption 60ml, 60 ℃ of following vacuum-dryings obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 1; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.14, with the solvent toluene proportioning be 1mol: 160ml, be 1: 0.30 with the chemical processing agent mol ratio.

Load type non-metallocene catalyst is designated as CAT-1-1.

Embodiment 1-2

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts aluminium sesquioxide.With aluminium sesquioxide lasting roasting 6h under 700 ℃, nitrogen atmosphere.Chemical processing agent changes titanium tetrabromide (TiBr into ₄).

Magnesium compound is changed into anhydrous magnesium bromide (MgBr ₂), the Nonmetallocene title complex adopts

The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into ethylbenzene; And with the mixed serum even heating to 110 that is obtained ℃, directly vacuumize drying then, obtain complex carrier; And then with titanium tetrabromide reaction, obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 4; In the Mg element; Magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.20; With solvent ethylbenzene proportioning be 1mol: 300ml, successively (obvious is that I is an elder generation with the chemical treatment reaction with the mol ratio of chemical processing agent; After with chemical treatment reaction II being, as follows) be respectively 1: 0.10 and 1: 0.20.

Load type non-metallocene catalyst is designated as CAT-1-2.

Embodiment 1-3

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts silica-magnesia mixed oxide (mass ratio 1: 1).The silica-magnesia mixed oxide is continued roasting 4h under 600 ℃, argon gas atmosphere.

Magnesium compound is changed into oxyethyl group magnesium chloride (MgCl (OC ₂H ₅)), chemical processing agent adopts tetraethyl-titanium (Ti (CH ₃CH ₂) ₄), the Nonmetallocene title complex adopts

The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into YLENE; And with the mixed serum even heating to 150 that is obtained ℃, directly vacuumize drying then, obtain complex carrier; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 0.5; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.05, with the solvent xylene proportioning be 1mol: 160ml, successively be respectively 1: 0.70 and 1: 0.10 with the mol ratio of chemical processing agent.

Load type non-metallocene catalyst is designated as CAT-1-3.

Embodiment 1-4

Basic identical with embodiment 1, but following change is arranged:

The porous support adopting montmorillonite.With polynite lasting roasting 8h under 400 ℃, nitrogen atmosphere.

Magnesium compound is changed into butoxy magnesium bromide (MgBr (OC ₄H ₉)), complex carrier is handled with chemical processing agent and is adopted tetra-n-butyl titanium (Ti (C ₄H ₉) ₄).The Nonmetallocene title complex adopts the solvent of

dissolved magnesium compound and Nonmetallocene title complex to change into diethylbenzene; And with the mixed serum even heating to 110 that is obtained ℃; Directly vacuumize drying then; Obtain complex carrier; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Wherein proportioning does; Magnesium compound and porous support mass ratio are 1: 10, and in the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.4; With solvent diethylbenzene proportioning be 1mol: 120ml, successively be respectively 1: 0.50 and 1: 0.20 with the mol ratio of chemical processing agent.

Load type non-metallocene catalyst is designated as CAT-1-4.

Embodiment 1-5

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts the PS of partial cross-linked (degree of crosslinking is 30%).This PS is continued oven dry 12h under 85 ℃, nitrogen atmosphere.

Magnesium compound is changed into methylmagnesium-chloride (Mg (CH ₃) Cl), the Nonmetallocene title complex adopts

The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into chlorotoluene; And with the mixed serum even heating to 120 that is obtained ℃, directly vacuumize drying then, obtain complex carrier; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Zirconium tetrachloride is adopted in the porous support chemical treatment, and complex carrier is handled and adopted titanium tetrachloride, and in the Mg element, magnesium compound and zirconium tetrachloride mol ratio are 1: 0.30, with the titanium tetrachloride mol ratio be 1: 0.25.

Load type non-metallocene catalyst is designated as CAT-1-5.

Embodiment 1-6

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts zeyssatite.With zeyssatite lasting roasting 8h under 500 ℃, nitrogen atmosphere.

Magnesium compound is changed into ethylmagnesium chloride (Mg (C ₂H ₅) Cl), the Nonmetallocene title complex adopts

And with the mixed serum even heating to 60 that is obtained ℃, directly vacuumize drying then, obtain complex carrier, so again with the chemical processing agent reaction, obtain load type non-metallocene catalyst.

Load type non-metallocene catalyst is designated as CAT-1-6.

Embodiment 1-7

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts molecular sieve ZSM-5.With molecular sieve lasting roasting 12h under 450 ℃, helium atmosphere.

Magnesium compound is changed into magnesium ethide (Mg (C ₂H ₅) ₂), the Nonmetallocene title complex adopts

Load type non-metallocene catalyst is designated as CAT-1-7.

Embodiment 1-8

Basic identical with embodiment 1, but following change is arranged:

Magnesium compound is changed into methyl ethoxy magnesium (Mg (OC ₂H ₅) (CH ₃)).

Load type non-metallocene catalyst is designated as CAT-1-8.

Embodiment 2

Porous support adopts silicon-dioxide, i.e. silica gel, and model is the ES757 of Ineos company, at first with silica gel lasting roasting 4h and thermal activation under 600 ℃, nitrogen atmosphere.

Chemical processing agent adopts titanium tetrachloride (TiCl ₄).Take by weighing the silica gel after the 5g thermal activation, add the 60ml hexane, under the stirring at normal temperature condition, add titanium tetrachloride,, filter at 60 ℃ down behind the reaction 2h, hexane wash 3 times, each 60ml, last vacuum is drained and is obtained modifying carrier.

Magnesium compound adopts Magnesium Chloride Anhydrous, and the solvent of dissolved magnesium compound and Nonmetallocene title complex adopts THF.It is the compound of

that the Nonmetallocene title complex adopts structure.

Take by weighing Magnesium Chloride Anhydrous and Nonmetallocene title complex, add behind the tetrahydrofuran solvent under the normal temperature fully that dissolving obtains magnesium compound solution, add then and modify carrier; Stir after 2 hours; With the mixed serum even heating to 90 that is obtained ℃, directly vacuumize drying then, obtain complex carrier.

Then in the complex carrier that is obtained, add the 60ml hexane; Under agitation condition, adopt triethyl aluminum (concentration is the hexane solution of 15wt%) to help chemical processing agent to handle complex carrier, with 30 minutes dropping triethyl aluminums, 60 ℃ of following stirring reactions were after 4 hours; Filter; Hexane wash 2 times, each hexane consumption 60ml, vacuum-drying under the normal temperature.

In the pre-treatment complex carrier that is obtained, add the 60ml hexane more then, under agitation condition with dripping titanium tetrachloride in 30 minutes, 60 ℃ of following stirring reactions 4 hours; Filter; Hexane wash 2 times, each hexane consumption 60ml, vacuum-drying obtains load type non-metallocene catalyst under the normal temperature.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 2; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.08, with the solvents tetrahydrofurane proportioning be 1mol: 240ml, with the triethyl aluminum mol ratio be 1: 0.15, be 1: 0.20 with twice chemical processing agent mol ratio.

Load type non-metallocene catalyst is designated as CAT-2.

Embodiment 2-1

Basic identical with embodiment 2, but following change is arranged:

Porous support is changed into 955 of Grace company, lasting roasting 8h under 400 ℃, nitrogen atmosphere and thermal activation.Chemical processing agent changes zirconium tetrachloride (ZrCl into ₄), hexane changes toluene into.Help chemical processing agent to change into MAO (MAO, the toluene solution of 10wt%).The Nonmetallocene title complex adopts the solvent of

dissolved magnesium compound and Nonmetallocene title complex to change into toluene; And with the mixed serum even heating to 100 that is obtained ℃, directly vacuumize drying then, obtain complex carrier; After helping chemical processing agent to handle; Then in this complex carrier, add 60ml toluene, under agitation condition with 30 minutes dropping zirconium tetrachlorides, 80 ℃ of following stirring reactions 4 hours; Filter; Toluene wash 2 times, each toluene consumption 60ml, 60 ℃ of following vacuum-dryings obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 1; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.14, with the solvent toluene proportioning be 1mol: 160ml, be 1: 0.15 with helping the chemical processing agent mol ratio, be 1: 0.30 with the chemical processing agent mol ratio.

Load type non-metallocene catalyst is designated as CAT-2-1.

Embodiment 2-2

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts aluminium sesquioxide.With aluminium sesquioxide lasting roasting 6h under 700 ℃, nitrogen atmosphere.Chemical processing agent changes titanium tetrabromide (TiBr into ₄).Help chemical processing agent to change into trimethylaluminium (Al (CH ₃) ₃)

Magnesium compound is changed into anhydrous magnesium bromide (MgBr ₂), the Nonmetallocene title complex adopts The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into ethylbenzene; And with the mixed serum even heating to 110 that is obtained ℃; Directly vacuumize drying then, obtain complex carrier, after helping chemical processing agent to handle; And then with titanium tetrabromide reaction, obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 4; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.20, with solvent ethylbenzene proportioning be 1mol: 300ml, be 1: 0.30 with helping the chemical processing agent mol ratio, successively be respectively 1: 0.10 and 1: 0.20 with the mol ratio of chemical processing agent.

Load type non-metallocene catalyst is designated as CAT-2-2.

Embodiment 2-3

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts silica-magnesia mixed oxide (mass ratio 1: 1).The silica-magnesia mixed oxide is continued roasting 4h under 600 ℃, argon gas atmosphere.Help chemical processing agent to change into triisobutyl aluminium (Al (i-C ₄H ₉) ₃).

Magnesium compound is changed into oxyethyl group magnesium chloride (MgCl (OC ₂H ₅)), the Nonmetallocene title complex adopts The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into YLENE; And with the mixed serum even heating to 150 that is obtained ℃; Directly vacuumize drying then, obtain complex carrier, after helping chemical processing agent to handle; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Wherein proportioning does, magnesium compound and porous support mass ratio are 1: 0.5; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.05, with the solvent xylene proportioning be 1mol: 160ml, be 1: 0.05 with helping the chemical processing agent mol ratio, successively be respectively 1: 0.70 and 1: 0.10 with the mol ratio of chemical processing agent.

Load type non-metallocene catalyst is designated as CAT-2-3.

Embodiment 2-4

Basic identical with embodiment 1, but following change is arranged:

The porous support adopting montmorillonite.With polynite lasting roasting 8h under 400 ℃, nitrogen atmosphere.

Magnesium compound is changed into butoxy magnesium bromide (MgBr (OC ₄H ₉)), help chemical processing agent to change into isobutyl aluminium alkoxide, the Nonmetallocene title complex adopts

The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into diethylbenzene; And with the mixed serum even heating to 110 that is obtained ℃; Directly vacuumize drying then, obtain complex carrier, after helping chemical processing agent to handle; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Wherein proportioning does; Magnesium compound and porous support mass ratio are 1: 10; In the Mg element, magnesium compound and Nonmetallocene title complex mol ratio are 1: 0.4, with solvent diethylbenzene proportioning be 1mol: 120ml; With helping the chemical processing agent mol ratio is 1: 0.50, successively is respectively 1: 0.50 and 1: 0.20 with the mol ratio of chemical processing agent.

Load type non-metallocene catalyst is designated as CAT-2-4.

Embodiment 2-5

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts the PS of partial cross-linked (degree of crosslinking is 30%).This PS is continued oven dry 12h under 85 ℃, nitrogen atmosphere.

Magnesium compound is changed into methylmagnesium-chloride (Mg (CH ₃) Cl), help chemical processing agent to change into diethylmethyl aluminium (Al (CH ₃) (CH ₃CH ₂) ₂), the Nonmetallocene title complex adopts

The solvent of dissolved magnesium compound and Nonmetallocene title complex is changed into chlorotoluene; And with the mixed serum even heating to 120 that is obtained ℃; Directly vacuumize drying then, obtain complex carrier, after helping chemical processing agent to handle; And then react with chemical processing agent again, obtain load type non-metallocene catalyst.

Zirconium tetrachloride is adopted in the porous support chemical treatment, and complex carrier is handled and adopted titanium tetrachloride, and in the Mg element, magnesium compound and zirconium tetrachloride mol ratio are 1: 0.30, are 1: 0.10 with helping the chemical processing agent mol ratio, with the titanium tetrachloride mol ratio be 1: 0.25.

Load type non-metallocene catalyst is designated as CAT-2-5.

Embodiment 2-6

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts zeyssatite.With zeyssatite lasting roasting 8h under 500 ℃, nitrogen atmosphere.

Magnesium compound is changed into ethylmagnesium chloride (Mg (C ₂H ₅) Cl), the Nonmetallocene title complex adopts

And with the mixed serum even heating to 60 that is obtained ℃, directly vacuumize drying then, obtain complex carrier, so again with the chemical processing agent reaction, obtain load type non-metallocene catalyst.

Load type non-metallocene catalyst is designated as CAT-2-6.

Embodiment 2-7

Basic identical with embodiment 1, but following change is arranged:

Porous support adopts molecular sieve ZSM-5.With molecular sieve lasting roasting 12h under 450 ℃, helium atmosphere.

Magnesium compound is changed into magnesium ethide (Mg (C ₂H ₅) ₂), the Nonmetallocene title complex adopts

Load type non-metallocene catalyst is designated as CAT-2-7.

Embodiment 2-8

Basic identical with embodiment 1, but following change is arranged:

Magnesium compound is changed into methyl ethoxy magnesium (Mg (OC ₂H ₅) (CH ₃)).

Load type non-metallocene catalyst is designated as CAT-2-8.

Reference example 1-A

Basic identical with embodiment 1, but following change is arranged:

Magnesium compound and Nonmetallocene title complex mol ratio are changed into 1: 0.16;

Load type non-metallocene catalyst is designated as CAT-1-A.

Reference example 1-B

Basic identical with embodiment 1, but following change is arranged:

Magnesium compound and Nonmetallocene title complex mol ratio are changed into 1: 0.04;

Load type non-metallocene catalyst is designated as CAT-1-B.

Reference example 1-C

Basic identical with embodiment 1, but following change is arranged:

Porous support is handled without chemical processing agent;

Load type non-metallocene catalyst is designated as CAT-1-C.

Reference example 1-D

Basic identical with embodiment 1, but following change is arranged:

Complex carrier is handled without chemical processing agent;

Load type non-metallocene catalyst is designated as CAT-1-D.

The application implementation example

The load type non-metallocene catalyst CAT-1 that makes in the embodiment of the invention, CAT-1-1～8, CAT-2, CAT-2～8, CAT-1-A～D are carried out the homopolymerization and the copolymerization of ethene respectively according to following method under following condition:

Homopolymerization is: 5 liters of polymerization autoclaves; Slurry polymerization processes, 2.5 liters of hexane solvents, polymerization stagnation pressure 0.8MPa; Hydrogen partial pressure 0.2MPa; 85 ℃ of polymerization temperatures are 100: 1 in the promotor of aluminium with mol ratio in the load type non-metallocene catalyst of central metal atom, 2 hours reaction times.At first 2.5 liters of hexanes are joined in the polymerization autoclave, open and stir, add 50mg load type non-metallocene catalyst and catalyst mixture then, continue to feed ethene and make the polymerization stagnation pressure constant at 0.8MPa.Reaction with gas reactor emptying, is emitted the still interpolymer after finishing, dry back weighing quality.The particular case of this polyreaction and polymerization evaluation result are as shown in table 1.

Copolymerization is: 5 liters of polymerization autoclaves; Slurry polymerization processes, 2.5 liters of hexane solvents, polymerization stagnation pressure 0.8MPa; Hydrogen partial pressure 0.2MPa; 85 ℃ of polymerization temperatures are 100: 1 in the promotor of aluminium with mol ratio in the load type non-metallocene catalyst of central metal atom, 2 hours reaction times.At first 2.5 liters of hexanes are joined in the polymerization autoclave; Open and stir; Add 50mg load type non-metallocene catalyst and catalyst mixture then, disposable adding 1-hexene co-monomer 50g and hydrogen continue to feed ethene and make the polymerization stagnation pressure constant in 0.8MPa to 0.2MPa.Reaction with gas reactor emptying, is emitted the still interpolymer after finishing, dry back weighing quality.The particular case of this polyreaction and polymerization evaluation result are as shown in table 1.

Table 1. load type non-metallocene catalyst is used for olefinic polyreaction effect table look-up

Visible by table 1, higher with the load type non-metallocene catalyst polymerization activity of method preparation provided by the invention, and polymer stacks density is also higher.

Test-results data through sequence number in the contrast table 11 and sequence number 12,13 can be known, increase or reduce Nonmetallocene title complex add-on in the catalyzer, and its activity increases thereupon or reduces, and the MWD of polymkeric substance also narrows down thereupon and broadens.Thereby explained that the Nonmetallocene title complex has the effect of the molecular weight distribution of narrowing in load type non-metallocene catalyst provided by the present invention, so can be through regulating the MWD that the relative proportioning with the complex carrier chemical processing agent of Nonmetallocene title complex is come telomerized polymer.

Sequence number 1 and 2,16 and 17 test-results data can be known in the contrast table 1, adopt load type non-metallocene catalyst provided by the invention, show significant comonomer effect, and promptly under equal relatively condition, the copolymerization activity is higher than the homopolymerization activity.

Test-results data through sequence number in the contrast table 11 and sequence number 14 can be known, adopt porous support provided by the present invention to handle the catalyst activity and the polymer stacks density that obtain through chemical processing agent and are higher than porous support without the resulting catalyzer of chemical processing agent.And the former resulting molecular weight distribution is wider than the latter, illustrates further thus, and method for preparing catalyst provided by the invention, chemical processing agent have the MWD and the effectiveness that improves polymer stacks density of wide fluidized polymer.

1～11 and 16～26 test-results data can be known in the contrast table 1; Complex carrier is after helping the chemical processing agent processing; But under analogy conditions, the polymerization catalyst activity is higher than without the catalyzer that helps chemical processing agent to handle, and molecular weight distribution is narrower than the latter slightly; The effect that helps chemical processing agent to have the increase catalyst activity and the molecular weight distribution that narrows is introduced in explanation thus in catalyst preparation process.

Though more than combined the embodiment specific embodiments of the invention to carry out detailed explanation, it is pointed out that protection scope of the present invention does not receive the restriction of these embodiments, but confirm by claims of appendix.Those skilled in the art can carry out suitable change to these embodiments in the scope that does not break away from technological thought of the present invention and purport, and these embodiments after changing obviously are also included within protection scope of the present invention.

Claims (13)

1. the preparation method of a load type non-metallocene catalyst may further comprise the steps:

Make the chemical processing agent and optional porous support reaction, the step that obtains to modify carrier that are selected from IV B family metallic compound through thermal activation treatment;

Magnesium compound is dissolved in the solvent, obtains the step of magnesium compound solution;

Said modification carrier, said magnesium compound solution are contacted with the Nonmetallocene title complex, obtain the step of mixed serum;

The said mixed serum of convection drying, the step of acquisition complex carrier; With

Make the chemical processing agent and the reaction of said complex carrier that are selected from said IV B family metallic compound, obtain the step of said load type non-metallocene catalyst.

2. according to the described preparation method of claim 1, also be included in and make before said chemical processing agent and the reaction of said complex carrier, with the step that helps the said complex carrier of chemical processing agent pre-treatment that is selected from aikyiaiurnirsoxan beta, aluminum alkyls or its arbitrary combination.

3. according to the described preparation method of claim 1; It is characterized in that; Said porous support is selected from the refractory oxide or in infusibility composite oxides, clay, molecular sieve, mica, polynite, wilkinite and the zeyssatite one or more of partial cross-linked form, periodic table of elements II A, III A, IV A or the IV B family metal of olefin homo or multipolymer, Z 150PH or its multipolymer, Schardinger dextrins, polyester or copolyesters, polymeric amide or copolyamide, ryuron or multipolymer, Voncoat R 3310 or multipolymer, methylacrylic acid ester homopolymer or multipolymer, styrene homopolymers or multipolymer, these homopolymer or multipolymer; Be preferably selected from partial cross-linked styrene polymer, silicon-dioxide, aluminum oxide, Natural manganese dioxide, oxidation sial, oxidation magnalium, titanium oxide, molecular sieve and the polynite one or more, more preferably be selected from silicon-dioxide.

4. according to the described preparation method of claim 1; It is characterized in that; Said magnesium compound is selected from one or more in magnesium halide, alkoxyl group magnesium halide, alkoxyl magnesium, alkyl magnesium, alkyl halide magnesium and the alkyl alkoxy magnesium, is preferably selected from the magnesium halide one or more, more preferably magnesium chloride.

5. according to the described preparation method of claim 1, it is characterized in that said solvent is selected from C _6-12Aromatic hydrocarbon, halo C _6-12In aromatic hydrocarbon, ester and the ether one or more are preferably selected from C _6-12In aromatic hydrocarbon and the THF one or more, most preferably THF.

6. according to the described preparation method of claim 1, it is characterized in that said Nonmetallocene title complex is selected from one or more in the compound with following chemical structural formula:

Be preferably selected from compound (A) with following chemical structural formula and in the compound (B) one or more:

More preferably be selected from compound (A-1) to compound (A-4) with following chemical structural formula and in compound (B-1) to the compound (B-4) one or more:

In above all chemical structural formulas,

Q is 0 or 1;

D is 0 or 1;

M is 1,2 or 3;

M is selected from periodic table of elements III family to XI family atoms metal, preferred IV B family atoms metal, more preferably Ti (IV) and Zr (IV);

N is 1,2,3 or 4, depends on the valence state of said central metal atom M;

X is selected from halogen, Wasserstoffatoms, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, nitrogen-containing group, sulfur-containing group, boron-containing group, contain aluminium base group, phosphorus-containing groups, silicon-containing group, germanic group or contain tin group, a plurality of X can be identical, also can be different, can also become key or Cheng Huan each other;

A be selected from Sauerstoffatom, sulphur atom, selenium atom, -NR ²³R ²⁴,-N (O) R ²⁵R ²⁶,

-PR ²⁸R ²⁹,-P (O) R ³⁰OR ³¹, sulfuryl, sulfoxide group or-Se (O) R ³⁹, wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

B is selected from nitrogen-atoms, nitrogen-containing group, phosphorus-containing groups or C ₁-C ₃₀Alkyl;

D is selected from nitrogen-atoms, Sauerstoffatom, sulphur atom, selenium atom, phosphorus atom, nitrogen-containing group, phosphorus-containing groups, C ₁-C ₃₀Alkyl, sulfuryl, sulfoxide group,

-N (O) R ²⁵R ²⁶, Or-P (O) R ³²(OR ³³), wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

E is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

F is selected from nitrogen-atoms, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

G is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Y is selected from Sauerstoffatom, nitrogen-containing group, oxy radical, sulfur-containing group, contain seleno group or phosphorus-containing groups, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

Z is selected from nitrogen-containing group, oxy radical, sulfur-containing group, contains seleno group, phosphorus-containing groups or cyanic acid, and wherein atom is used in N, O, S, Se and the P coordination of respectively doing for oneself;

→ represent singly-bound or two key;

-represent covalent linkage or ionic linkage;

---represent co-ordination bond, covalent linkage or ionic linkage;

R ¹To R ⁴, R ⁶To R ³⁶, R ³⁸And R ³⁹Be selected from hydrogen, C independently of one another ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group, above-mentioned group can be the same or different to each other, and wherein adjacent group can combine togather into key or Cheng Huan, is preferably formed aromatic ring, and

R ⁵Be selected from lone-pair electron on the nitrogen, hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl, oxy radical, sulfur-containing group, nitrogen-containing group, contain seleno group or phosphorus-containing groups; Work as R ⁵For oxy radical, sulfur-containing group, nitrogen-containing group, when containing seleno group or phosphorus-containing groups, R ⁵In N, O, S, P and Se can be used as coordination and carry out coordination with atom and said center IV B family atoms metal,

Said Nonmetallocene title complex further is preferably selected from one or more in the compound with following chemical structural formula:

Most preferably be selected from the compound with following chemical structural formula one or more:

7. according to the described preparation method of claim 6, it is characterized in that,

Said halogen is selected from F, Cl, Br or I;

Said nitrogen-containing group is selected from -NR ²³R ²⁴,-T-NR ²³R ²⁴Or-N (O) R ²⁵R ²⁶

Said phosphorus-containing groups is selected from

-PR ²⁸R ²⁹,-P (O) R ³⁰R ³¹Or-P (O) R ³²(OR ³³);

Said oxy radical be selected from hydroxyl ,-OR ³⁴With-T-OR ³⁴

Said sulfur-containing group is selected from-SR ³⁵,-T-SR ³⁵,-S (O) R ³⁶Or-T-SO ₂R ³⁷

The said seleno group that contains is selected from-SeR ³⁸,-T-SeR ³⁸,-Se (O) R ³⁹Or-T-Se (O) R ³⁹

Said group T is selected from C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Said R ³⁷Be selected from hydrogen, C ₁-C ₃₀Alkyl, substituted C ₁-C ₃₀Alkyl or safing function property group;

Said C ₁-C ₃₀Alkyl is selected from C ₁-C ₃₀Alkyl, C ₇-C ₅₀Alkaryl, C ₇-C ₅₀Aralkyl, C ₃-C ₃₀Cyclic alkyl, C ₂-C ₃₀Thiazolinyl, C ₂-C ₃₀Alkynyl, C ₆-C ₃₀Aryl, C ₈-C ₃₀Condensed ring radical or C ₄-C ₃₀Heterocyclic radical, wherein said heterocyclic radical contain 1-3 heteroatoms that is selected from nitrogen-atoms, Sauerstoffatom or sulphur atom;

Said substituted C ₁-C ₃₀Alkyl is selected from and has one or more aforementioned halogens or aforementioned C ₁-C ₃₀Alkyl is as substituent aforementioned C ₁-C ₃₀Alkyl;

Said safing function property group is selected from aforementioned halogen, aforementioned oxy radical, aforementioned nitrogen-containing group, silicon-containing group, germanic group, aforementioned sulfur-containing group, contains tin group, C ₁-C ₁₀Ester group or nitro,

Wherein, said boron-containing group is selected from BF ₄ ^-, (C ₆F ₅) ₄B ^-Or (R ⁴⁰BAr ₃) ^-

Saidly contain aluminium base group and be selected from aluminum alkyls, AlPh ₄ ^-, AlF ₄ ^-, AlCl ₄ ^-, AlBr ₄ ^-, AlI ₄ ^-Or R ⁴¹AlAr ₃ ^-

Said silicon-containing group is selected from-SiR ⁴²R ⁴³R ⁴⁴Or-T-SiR ⁴⁵

Said germanic group is selected from-GeR ⁴⁶R ⁴⁷R ⁴⁸Or-T-GeR ⁴⁹

Saidly contain tin group and be selected from-SnR ⁵⁰R ⁵¹R ⁵²,-T-SnR ⁵³Or-T-Sn (O) R ⁵⁴,

Said Ar represents C ₆-C ₃₀Aryl, and

R ⁴⁰To R ⁵⁴Be selected from hydrogen, aforementioned C independently of one another ₁-C ₃₀Alkyl, aforementioned substituted C ₁-C ₃₀Alkyl or aforementioned safing function property group, wherein these groups can be the same or different to each other, and wherein adjacent group can combine togather into key or Cheng Huan, and said group T ditto defines.

8. according to the described preparation method of claim 1, it is characterized in that, is 1 in the said magnesium compound of Mg element and the mol ratio of said Nonmetallocene title complex: 0.01-1; Preferred 1: 0.04-0.4, more preferably 1: 0.08-0.2, the ratio of said magnesium compound and said solvent is 1mol: 75～400ml; Preferred 1mol: 150～300ml; More preferably 1mol: 200～250ml is 1 in the said magnesium compound of magnesium compound solid and the mass ratio of said porous support: 0.1-20, preferred 1: 0.5-10; More preferably 1: 1-5; And is respectively 1 in the said magnesium compound of Mg element independently of one another with mol ratio in the said chemical processing agent of IV B family metallic element: 0.01-1, preferred 1: 0.01-0.50, more preferably 1: 0.10-0.30.

9. according to the described preparation method of claim 1; It is characterized in that; Said IV B family metallic compound is selected from one or more in IV B family metal halide, IV B family metal alkyl compound, IV B family metal alkoxide compound, IV B family metal alkyl halides and the IV B family metal alkoxide halogenide; Be preferably selected from the IV B family metal halide one or more, more preferably be selected from TiCl ₄, TiBr ₄, ZrCl ₄, ZrBr ₄, HfCl ₄And HfBr ₄In one or more, most preferably be selected from TiCl ₄And ZrCl ₄In one or more.

10. according to the described preparation method of claim 2; It is characterized in that; Said aikyiaiurnirsoxan beta is selected from one or more in MAO, ethyl aikyiaiurnirsoxan beta, isobutyl aluminium alkoxide and the normal-butyl alumina alkane; More preferably be selected from MAO and the isobutyl aluminium alkoxide one or more; And said aluminum alkyls is selected from trimethylaluminium, triethyl aluminum, tri-propyl aluminum, triisobutyl aluminium, three n-butylaluminum, triisopentyl aluminium, three n-pentyl aluminium, three hexyl aluminium, three isohexyl aluminium, diethylmethyl aluminium and the dimethyl ethyl aluminium one or more; Be preferably selected from trimethylaluminium, triethyl aluminum, tri-propyl aluminum and the triisobutyl aluminium one or more, most preferably be selected from triethyl aluminum and the triisobutyl aluminium one or more.

It 11., it is characterized in that, is 1 with helping the mol ratio of chemical processing agent: 0-1.0, preferred 1: 0-0.5, more preferably 1: 0.1-0.5 in Al element said in the said magnesium compound of Mg element according to the described preparation method of claim 2.

12. a load type non-metallocene catalyst, it is by making according to each described preparation method of claim 1-11.

13. alkene homopolymerization/copolymerization process; It is characterized in that; Being Primary Catalysts according to the described load type non-metallocene catalyst of claim 12; To be selected from aikyiaiurnirsoxan beta, aluminum alkyls, haloalkyl aluminium, boron fluothane, boron alkyl and the boron alkyl ammonium salt one or more is promotor, makes alkene homopolymerization or copolymerization.