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Self-limiting catalyst composition with bidentate internal donor

Self-limiting catalyst composition with bidentate internal donor
IPC classes for russian patent Self-limiting catalyst composition with bidentate internal donor (RU 2489447):
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Thermoplastic polyolefins with high fluidity and excellent surface quality, obtained in multistep process Thermoplastic polyolefins with high fluidity and excellent surface quality, obtained in multistep process / 2470963
Invention provides reactor thermoplastic polyolefins having high fluidity and excellent surface quality, which contain (A) a matrix of a propylene homo- or copolymer whose weight ratio ranges from 40 to 90% with ISO 1133 MFR index (230°C, nominal load of 2.16 kg)≥200 g/10 min, and (B) an elastomeric copolymer of ethylene and propylene whose weight ratio ranges from 2 to 30%, with characteristic viscosity of IV (according to ISO 1628 in decalin as a solvent)≤2.8 dl/g with weight ratio of ethylene ranging from more than 50 to 80% and (C) an elastomeric copolymer of ethylene and propylene whose weight ratio ranges from 8 to 30%, with characteristic viscosity IV (according to ISO 1628 in decalin as a solvent) ranging from 3.0 to 6.5 dl/g and with weight content of propylene ranging from 50 to 80%. The reactor thermoplastic polyolefins are obtained in a process by multistep polymerisation, involving at least 3 successive steps, in the presence of a catalyst comprising (i) a Ziegler-Natta procatalyst which contains a product of transesterification of a lower alcohol and a phthalic ester of complex acids, (ii) an organometallic cocatalyst and (iii) an external donor of formula (I), Si(OCH2CH3)3(NR1R2), where values of R1 and R2 are given in the claim. The invention also discloses a multistep process of producing said polyolefins, involving either a combination of one loop reactor and two or three gas-phase reactors, or a combination of two loop reactors and two gas-phase reactors, connected in series. Disclosed polyolefins are used to produce articles for the automobile industry by pressure casting. The invention also relates to articles moulded from the reactor thermoplastic polyolefins.
Self-limiting catalyst system with controlled aluminium to sca ratio and method Self-limiting catalyst system with controlled aluminium to sca ratio and method / 2470947
Catalyst composition contains: one or more Ziegler-Natta procatalyst compositions having one or more transition metal compounds and one or more internal electron donors in form of esters of aromatic dicarboxylic acid, one or more aluminium-containing cocatalysts and a selectivity control agent (SCA) which contains a mixture of (i) a first alkoxy silane and a second alkoxy silane and (ii) an ester of C4-C30-aliphatic acid, and the molar ratio of aluminium to total SCA ranges from 0.5:1 to 4:1.
High-purity heterophase propylene copolymers High-purity heterophase propylene copolymers / 2470946
Invention relates to a catalyst system, production and use of high-purity heterophase propylene copolymers which contain (A) a matrix of a propylene homo- or copolymer whose weight ratio ranges from 73 to 98%, with ISO 1133 MFR2 index ≥45 g/10 min and (B) an elastomeric copolymer whose weight ratio ranges from 2 to 27%, wherein the weight ratio of propylene is at least 50% of component (B) and weight ratio of ethylene and/or any other C4-C10 alpha-olefin is at least 50% of component (B). Propylene copolymers are obtained during multi-step polymerisation in the presence of the catalyst system, including (i) a Ziegler-Natta procatalyst which contains a product of transesterificatin of a lower alcohol and a phthalic ester of complex acids, and (ii) possibly an organometallic cocatalyst, and (iii) an external donor of formula (I) Si(OCH2CH3)3(NR1R2), where elements R1 and R2 can be the same or different hydrocarbon groups, each containing 1-12 carbon atoms. The copolymers are used to produce moulded articles.
Self-limiting catalyst composition with no silane Self-limiting catalyst composition with no silane / 2461578
Described is a catalyst composition including one or more Ziegler-Natta procatalyst compositions containing one or more transition metal compounds and an internal electron donor, one or more aluminium containing cocatalysts, and a selectivity control agent (SCA), which contains a mixture of a carboxylic acid ester and a compound which does not contain silane, selected from the group consisting of a diether compound, a succinate compound, a piperidine compound and combinations thereof.
Catalyst system for producing polypropylene copolymers Catalyst system for producing polypropylene copolymers / 2436800
Described is a catalyst system for producing propylene copolymers, in which the weight ratio of the comonomer to the sum of monomers present in said polypropylene copolymer (comonomer/(comonomer + propylene)) is equal to at least 2.0 wt %, containing (a) procatalyst composition containing (i) a group 4-6 transition metal compound (IUPAC, Nomenclature of inorganic chemistry, 1989), (ii) MgCl2 and (iii) an intrinsic donor in which said intrinsic donor contains diethyl phthalate, and (b) an extrinsic donor which is diisopropyl diethoxy silane (DIPDES), and (c) an organometallic cocatalyst. The invention describes a method of producing the described catalyst system in which a procatalyst is obtained at the first step and an extrinsic donor and a cocatalyst are added at the second step. The invention also describes propylene copolymers obtained in the presence of the described catalyst system.
Magnesium dichloride-containing adducts and catalytic components obtained with them Magnesium dichloride-containing adducts and catalytic components obtained with them / 2342998
Described are solid Lewis adducts, containing MgCl2, Lewis base (LB), belonging to simple ethers, complex alkyl esters of C1-C10 aliphatic carboxylic acids, ketones, silanes or amines, and alcohol ROH, where R represents C1-C15 carbon group, optionally substituted with heteroatom-containing groups, said compounds being in molar ratio with each other, which is determined by the following formula MgCl2(ROH)m(LB)n(H2O)p, in which m lies in interval from 0.05 to 6, n lies in interval from 0.08 to 6 and p lies in interval from 0.01 to 0.6. Also described is method of obtaining said solid Lewis adduct, including (i) contacting of MgCl2, alcohol ROH and Lewis base LB optionally in presence of inert liquid thinner; (ii) heating of system to temperature of mixture melting and sustaining said conditions in order to obtain fully melted adduct; and (iii) quick cooling of melted adduct and obtaining as a result its hardening; also described are catalytic components obtained during contacting of described above adducts with compounds of titanium of formula Ti(OR)nXy-n, where n equals from 0 to y, y represents titanium valency, X represents halogen and R represents alkyl radical, which has 1-10 carbon atoms, or COR group, and containing electron donor, selected from complex esters, simple ethers, amines and ketones; described is catalytic system for alpha-olefin polymerisation and method of olefin polymerisation.
Highstereoregular polypropylene with improved properties Highstereoregular polypropylene with improved properties / 2325404
Invention refers to crystalline propylene polymers with high stereoregularity, specifically high content of isotactic pentalogies, improved processability in molten state and to production method. Propylene polymer is produced with the following properties: isotactic pentalogies content, measured by nuclear magnetic resonance (NMR), is higher than 98%, chain-length distribution expressed by ratio is from 6 to 11, and value of ratio is equal or lower than 5.5. Specified polymer is produced with special combination of solid components of Zigler-Natt catalyst and highstereoregular electron-donor compounds. Film or plate is made of propylene polymers having said properties. Sandwiched laminated product comprises specified film or plate. Films and plate are characterized by good homogeneous thickness, as well as high ultimate elongation and high ultimate tensile strength.
Catalytic components for polymerization of olefins / 2322457
Invention provides solid catalytic component for polymerization of olefins, contains magnesium, titanium, halogen, and electronodonor compound belonging to series of ethers, esters, amines, ketones, or nitriles and is characterized by Mg/Ti molar ratio higher than 5 and electronodonor compound-to-titanium molar ratio higher than 3.5, while titanium atoms originate from titanium tetrahalides or compounds of formula TiXn(OR1)4-n wherein 0≤n≤3, X represents halogen and R C1-C10-hydrocarbon group and wherein magnesium atoms originate from adduct of formula MgCl2•pR2OH wherein p represents number from 0.1 to 6 and R2 C1-C18-hydrocarbon radical. Also described is olefin polymerization catalyst containing product obtained by contacting above solid catalytic component, one or several alkylaluminum compound, and optionally an external electronodonor compound optionally followed by pre-polymerization with one or several olefins of formula CH2=CHR, wherein R is H or C1-C10-hydrocarbon group, to form polymer in amount from about 0.1 to about 1000 g per 1 g of solid catalytic component. Further described is copolymerization of olefins CH2=CHR, wherein R is H or C1-C10-hydrocarbon group, in presence of proposed catalyst.
Components of catalyst for polymerization of olefins, catalyst, method for preparing propylene polymers and propylene polymer Components of catalyst for polymerization of olefins, catalyst, method for preparing propylene polymers and propylene polymer / 2279442
Invention relates to the catalyst component used in polymerization of olefins comprising Mg, Ti, halogen and at least two electron-donor compounds wherein indicated catalyst component and at least one of electron-donor compounds repenting in the amount in the range from 20 to 50 mole% with respect to the complete amount of donors are chosen from succinic acid esters that are not extractable by above 25 mole% and at least one additional electron-donor compound that is extractable by above 35 mole%. Indicated components of catalyst provides preparing polymers possessing good insolubility level in xylene, high content level of stereoblocks and broad MWD value that is suitable for preparing polymers used in the region using bi-oriented polypropylene films. Also, invention relates to catalyst used in polymerization of olefins, methods for preparing propylene polymers and propylene polymer.
Supported ethylene (co) / 2258711
High-activity ethylene (co)polymerization-appropriate supported titanium-based catalyst is composed of (A) supported catalytic component, notably titanium-containing active component on porous silica, containing at least one titanium compound, at least one magnesium compound, at least one alkylaluminum compound, at least one halide promoter, at least one electron-donor compound, and inert porous silica carrier, wherein halide promoter belongs to the class of compounds described by general formula F-R1[R2bX(3-b)], in which F represents oxygen-containing functional group reactive to organoaluminum compound, titanium compound, and hydroxyl groups; R1 bivalent C1-C6-aliphatic or aromatic grouplinked to functional group F; R2 hydrogen atom, unsubstituted or halogen-substituted C1-C6-alkyl, halogen-substituted C3-C6-cycloalkyl, or halogen-substituted C6-C10-aryl; b=0,1 or 2; and X represents fluorine, chlorine, or bromine atom; and (B) alkylaluminum cocatalyst. Invention also discloses catalyst preparation method and ethylene (co)polymerization process in presence of above-defined catalyst.
High melt flow rate, impact-resistant propylene copolymer and method for production thereof High melt flow rate, impact-resistant propylene copolymer and method for production thereof / 2487897
Polymerisation method involves contacting propylene and optionally at least one other olefin with a catalyst composition in a first polymerisation reactor under gas-phase polymerisation conditions, the catalyst composition containing a procatalyst, a cocatalyst and a mixed external electron donor (M-EED) containing a first selectivity control agent (SCA1), a second selectivity control agent (SCA2), and an activity limiting agent (ALA); forming, in a first polymerisation reactor, an active propylene-based polymer having a melt flow rate greater than about 100 g/10 min as measured in accordance with ASTM D1238-01 (230°C, 2.16 kg); contacting the active propylene-based polymer with at least one olefin in a second reactor under polymerisation conditions; and obtaining an impact-resistant propylene copolymer having a melt flow rate greater than about 60 g/10 min. A version of the method and the polymer is disclosed.
Method of producing high-fluidity propylene polymers Method of producing high-fluidity propylene polymers / 2471811
Invention relates to a method of producing propylene polymers. The obtained propylene polymer has melt flow rate (230°C, 2.16 kg) higher than 30 g/10 min. The method is realised in the presence of a catalyst system comprising (a) a solid catalyst component containing Mg, Ti, halogen and an electron donor compound selected from succinates; (b) an alkylaluminium cocatalyst; and (c) a silicon compound of formula R1Si(OR)3, in which R1 is a branched alkyl and R is independently a C1-C10 alkyl. A method of producing a propylene polymer composition and heterophase compositions is also described.
Thermoplastic polyolefins with high fluidity and excellent surface quality, obtained in multistep process Thermoplastic polyolefins with high fluidity and excellent surface quality, obtained in multistep process / 2470963
Invention provides reactor thermoplastic polyolefins having high fluidity and excellent surface quality, which contain (A) a matrix of a propylene homo- or copolymer whose weight ratio ranges from 40 to 90% with ISO 1133 MFR index (230°C, nominal load of 2.16 kg)≥200 g/10 min, and (B) an elastomeric copolymer of ethylene and propylene whose weight ratio ranges from 2 to 30%, with characteristic viscosity of IV (according to ISO 1628 in decalin as a solvent)≤2.8 dl/g with weight ratio of ethylene ranging from more than 50 to 80% and (C) an elastomeric copolymer of ethylene and propylene whose weight ratio ranges from 8 to 30%, with characteristic viscosity IV (according to ISO 1628 in decalin as a solvent) ranging from 3.0 to 6.5 dl/g and with weight content of propylene ranging from 50 to 80%. The reactor thermoplastic polyolefins are obtained in a process by multistep polymerisation, involving at least 3 successive steps, in the presence of a catalyst comprising (i) a Ziegler-Natta procatalyst which contains a product of transesterification of a lower alcohol and a phthalic ester of complex acids, (ii) an organometallic cocatalyst and (iii) an external donor of formula (I), Si(OCH2CH3)3(NR1R2), where values of R1 and R2 are given in the claim. The invention also discloses a multistep process of producing said polyolefins, involving either a combination of one loop reactor and two or three gas-phase reactors, or a combination of two loop reactors and two gas-phase reactors, connected in series. Disclosed polyolefins are used to produce articles for the automobile industry by pressure casting. The invention also relates to articles moulded from the reactor thermoplastic polyolefins.
Self-limiting catalyst system with controlled aluminium to sca ratio and method Self-limiting catalyst system with controlled aluminium to sca ratio and method / 2470947
Catalyst composition contains: one or more Ziegler-Natta procatalyst compositions having one or more transition metal compounds and one or more internal electron donors in form of esters of aromatic dicarboxylic acid, one or more aluminium-containing cocatalysts and a selectivity control agent (SCA) which contains a mixture of (i) a first alkoxy silane and a second alkoxy silane and (ii) an ester of C4-C30-aliphatic acid, and the molar ratio of aluminium to total SCA ranges from 0.5:1 to 4:1.
High-purity heterophase propylene copolymers High-purity heterophase propylene copolymers / 2470946
Invention relates to a catalyst system, production and use of high-purity heterophase propylene copolymers which contain (A) a matrix of a propylene homo- or copolymer whose weight ratio ranges from 73 to 98%, with ISO 1133 MFR2 index ≥45 g/10 min and (B) an elastomeric copolymer whose weight ratio ranges from 2 to 27%, wherein the weight ratio of propylene is at least 50% of component (B) and weight ratio of ethylene and/or any other C4-C10 alpha-olefin is at least 50% of component (B). Propylene copolymers are obtained during multi-step polymerisation in the presence of the catalyst system, including (i) a Ziegler-Natta procatalyst which contains a product of transesterificatin of a lower alcohol and a phthalic ester of complex acids, and (ii) possibly an organometallic cocatalyst, and (iii) an external donor of formula (I) Si(OCH2CH3)3(NR1R2), where elements R1 and R2 can be the same or different hydrocarbon groups, each containing 1-12 carbon atoms. The copolymers are used to produce moulded articles.
Catalyst for polymerisation and copolymerisation of ethylene, preparation method thereof and method of producing polyethylenes using said catalyst Catalyst for polymerisation and copolymerisation of ethylene, preparation method thereof and method of producing polyethylenes using said catalyst / 2462479
Catalyst contains tetracyclopentadienyl zirconium (C5H5)4Zr, aluminoxane, a polyalkyl derivative of a nontransition metal MtRn, where Mt is a group IIA-IVA nontransition metal, and R = CH3, C2H5, C3H7, C4H9, iso-C4H9, C8H17; and/or titanium tetraalkoxide. The catalyst can have a support selected from a group comprising silica gel, ash from burning rice husks, kaolin or diatomite. The catalyst is biphase and contains a solid and liquid phase. The solid phase is metallocene and aluminoxane pre-deposited on the support, and the liquid phase is a solution of titanium tetraalkoxide in an aliphatic or aromatic solvent. Medium- or low-density polyethylenes are obtained in the presence of said catalyst. Medium and low-density polyethylene with given molecular weight, molecular-weight distribution and branching is obtained by varying the molar ratio titanium alkoxide/metallocene and MtRn/metallocene in the catalyst.
Catalyst systems and polymerisation processes Catalyst systems and polymerisation processes / 2452740
Invention relates to an olefin polymerisation method using multimodal catalyst systems, a method of monitoring ageing of a multimodal catalyst system and to a container or a reservoir. The first method involves (a) preparation of a catalyst system comprising a bisamide catalyst system and a non-bisamide catalyst system; (b) storing the multimodal catalyst system at controlled temperature lower than 1°C; (c) bringing the multimodal catalyst system into contact with C2-C4-alpha-olefin during a polymerisation process; and (d) obtaining a multimodal polymer. The second method involves (a) preparation of said catalyst system; and b) transporting said system in a portable reservoir, where the portable reservoir is kept at controlled temperature lower than 1°C or -9°C. The container or reservoir contains a multimodal catalyst system kept at the controlled temperature. The disclosed group of inventions enables to minimise loss of efficiency of the catalyst system during storage/ageing.
Catalyst system for producing polypropylene copolymers Catalyst system for producing polypropylene copolymers / 2436800
Described is a catalyst system for producing propylene copolymers, in which the weight ratio of the comonomer to the sum of monomers present in said polypropylene copolymer (comonomer/(comonomer + propylene)) is equal to at least 2.0 wt %, containing (a) procatalyst composition containing (i) a group 4-6 transition metal compound (IUPAC, Nomenclature of inorganic chemistry, 1989), (ii) MgCl2 and (iii) an intrinsic donor in which said intrinsic donor contains diethyl phthalate, and (b) an extrinsic donor which is diisopropyl diethoxy silane (DIPDES), and (c) an organometallic cocatalyst. The invention describes a method of producing the described catalyst system in which a procatalyst is obtained at the first step and an extrinsic donor and a cocatalyst are added at the second step. The invention also describes propylene copolymers obtained in the presence of the described catalyst system.
Combination of catalysts containing support materials, characterised by improved particle size distribution Combination of catalysts containing support materials, characterised by improved particle size distribution / 2412204
Method involves bringing hydrogen and ethylene monomers into contact with a composition deposited on a catalyst support based on several transition metals to obtain a polyolefin composition; where the composition deposited on the catalyst support based on several transition metals contains: (a) at least two catalyst components selected from a group consisting of: non-metallocene catalyst component which is a Ziegler-Natta catalyst, and a metallocene catalyst component of formula CpACpBMXp and CpA(A)CpBMXp, where each of CpA and CpB is identical or different and is unsubstituted or substituted with a cyclopentadienyl ring, each of which is bonded with M; M is an atom of a group 4 element; X is selected from a group consisting of C1-C6 alkyls, C6 aryls, C7-C12 alkylaryls, fluorinated C1-C6 alkyls, fluorinated C6 aryls, fluorinated C7-C12 alkylaryls, chlorine and fluorine; n equals 1 or 2; (A) denotes a divalent bridging group; and at least one X denotes fluorine or fluorinated hydrocarbonyl; (b) support material which is characterised by D50 value less than approximately 30 micrometres, and particle size distribution characterised by ratio D90/D10 less than approximately 5; and (c) an activator. The invention also discloses a composition deposited on the catalyst support, a polymer and a film.
Catalyst composition, containing shuttle agent, for formation of multi-block-copolymer of higher olefin Catalyst composition, containing shuttle agent, for formation of multi-block-copolymer of higher olefin / 2375381
Invention relates to compositions for polymerisation of propylene, 4-methyl-1-pentene, styrene or some other C4-8 α-olefin and one or more copolymers. The invention relates to a multi-block-copolymer, formed through polymerisation of propylene, 4-methyl-1-pentene, styrene or some other C4-20 α-olefin and a copolymerised comonomer in the presence of a composition, which contains a mixture or a reaction product obtained from combining: (A) first catalyst for polymerisation of olefins, (B) second catalyst for polymerisation of olefins, which enables production of polymers, distinguished by chemical or physical properties from the polymer obtained with catalyst (A) in equivalent polymerisation conditions, and (C) a chain shuttle agent, where (A) or has formula: where: T3 is a divalent bridge group of 2 to 20 atoms, excluding hydrogen, and Ar2, independently in each case, is arylene or alkyl- or aryl-substituted arylene group from 6 to 20 atoms, excluding hydrogen, M3 is a group IV metal, G, independently in each case, is an anion, neutral or dianion ligand-group, g is an integer from 1 to 5, which indicates the number of such G groups, and electron-donor reactions are shown by arrows, or has formula: , where M3 is Hf or Zr; Ar4 is C6-20 aryl or its inert substituted derivatives, especially 3,5-di(isopropyl)phenyl, 3,5-di(isobutyl)phenyl, dibenzo-1H-pyrrol-1-yl or anthracen-5-yl and T4, independently in each case, contains C3-6 alkylene group, C3-6 cycloalkylene group or their inert substituted derivatives; R21, independently in each case, is hydrogen, halogen, hydrocarbyl, trihydrocarbylsilyl or trihydrocarbylsilylhydrocarbyl from up to 50 atoms, excluding hydrogen; and G, independently in each case, is halogen or hydrocarbyl or trihydrocarbylsilyl group from up to 20 atoms, excluding hydrogen, or 2 G groups together represent a divalent derivative of the said hydrocarbyl or trihydrocarbylsily groups. The invention also relates to a method of producing the said multi-block-copolymer, to its functionalised or cross linked derivatives and polymer mixture containing it.
Regenerated catalyst for hydrofining hydrocarbon material, method of regenerating deactivated catalyst and process of hydrofining hydrocarbon material / 2484896
Invention relates to a regenerated hydrofining catalyst, a method of regenerating deactivated catalysts and a method of hydrofining oil distillates. Described is a regenerated catalyst for hydrofining hydrocarbon material, having pore volume of 0.3-0.8 ml/g, specific surface area of 150-280 m2/g, average pore diameter of 6-15 nm, which contains molybdenum, cobalt or nickel, sulphur and a support, wherein the molybdenum, cobalt or nickel is contained in the catalyst in form of nitrate complexes of compounds Co(C6H6O7), Ni(C6H6O7), H4[Mo4(C6H5O7)2O11], and the sulphur is contained in form of a sulphate anion SO4-2 in the following concentrations, wt %: Co(C6H6O7) or Ni(C6H6O7) - 7.3-16.6; H4[Mo4(C6H5O7)2O11] - 17.3-30.0; SO4-2 - 0.25-2.70; support - the balance; cobalt or nickel citrates can be coordinated to molybdenum citrate. Described is a method of regenerating a catalyst for hydrofining hydrocarbon material according to which a deactivated catalyst is fired and then saturated with citric acid solution and the dried in conditions which enable to obtain the catalyst described above. Described is a method of hydrofining hydrocarbon material at temperature of 320-400°C, pressure 0.5-10 MPa, weight flow rate of material of 0.5-5 h-1, volume ratio hydrogen/material equal to 100-1000 m3/m3 in the presence of the catalyst described above.

FIELD: chemistry.

SUBSTANCE: catalyst composition contains: one or more Ziegler-Natta procatalyst compositions having one or more transition metal compounds and an internal electron donor, containing a bidentate compound having at least two oxygen-containing functional groups which are separated by at least one saturated C2-C10 hydrocarbon chain; one or more aluminium-containing cocatalysts; and an external electron donor containing a mixture of a selectivity determining agent, selected from a group consisting of an alkoxy silane composition and a diether, and an activity limiting agent, selected from a group consisting of an ester of an aromatic mono- or polycarboxylic acid and a fatty acid ester.

EFFECT: catalyst composition does not require use of a phthalate-based internal electron donor and has high stereoselectivity and is self-extinguishing.

10 cl, 3 ex, 1 tbl

 

CROSS-REFERENCE TO RELATED APPLICATION

The present application claims the priority of patent application U.S. serial number 61/015978, filed December 21, 2007, the full contents of which by reference is incorporated herein.

BACKGROUND of the INVENTION

The present description relates to compositions stereoselective catalyst of Ziegler-Natta, intended for use in the polymerization and, in particular, polymerization of propylene.

As you know, adding a silanol composition to the catalyst system of the Ziegler-Natta containing talaty internal electron donor, improves the selectivity of the catalyst. Mixing a silanol composition with an agent that limits activity, (AAO), such as an ester of an aromatic carboxylic acid, optionally attached to the catalyst system of the Ziegler-Natta property of fire extinguishing. Modern studies indicate the growing concern over health risks associated with phthalates. It would be desirable to develop other systems of the catalysts of the Ziegler-Natta, providing control of selectivity, which are self-extinguishing and do not require the use of an internal electron donor on phthalates basis.

SUMMARY of INVENTION

The present description the invention relates to compositions of catalysts, demonstrating high catalyst activity and high stereoselectivity, and which is self-extinguishing. The present composition of the catalysts do not require the use of an internal electron donor on phthalates basis.

In one embodiment, the implementation of the proposed composition of the catalyst. The catalyst composition includes one or more compositions of proletarization Ziegler-Natta containing one or more transition metal compounds and an internal electron donor. The internal electron donor is a bidentate compound. The composition of the catalyst also contains the aluminium-containing socialization. The catalyst composition further comprises an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity.

Bidentate compound has at least two oxygen-containing functional groups with oxygen-containing functional groups separated by at least one saturated With2-C10hydrocarbon chain, which optionally may contain heteroatom (heteroatoms). Bidentate connection eliminates phthalates. Bidentate compound can be simple fluids, succinate, glutarate, dialkoxybenzene, bis(alkoxyphenyl is), ester diol complex alkoxyalkyl ether, and any combination thereof.

In one embodiment, the implementation of the proposed composition of the catalyst. The catalyst composition includes one or more compositions of proletarization Ziegler-Natta. The composition of pronatalistic contains one or more transition metal compounds and an internal electron donor, which is a simple fluids. The composition of pronatalistic also contains one or more of aluminium-containing socialization. The catalyst composition further comprises an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity.

In one embodiment, the implementation of simple fluids may represent a 2,2-Diisobutyl-1,3-dimethoxypropane, 2,2-dicyclopentyl-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane or 9,9-bis(methoxymethyl)fluorene. The agent that determines the selectivity, can be alkoxysilane composition or simple fluids. Alkoxysilane the composition may be an n-propyltrimethoxysilane, dicyclopentadienyliron or methylcyclohexanecarboxylic or a mixture of alkoxysilanes containing n-propyltrimethoxysilane, dicyclopentadienyliron and/or methylcyclohexylamine the silane. The agent that determines the selectivity can also be simple fluids, which may be identical or different in comparison with the previously described simple fluids, which is the internal electron donor, such as 2,2-dicyclopentyl-1,3-dimethoxypropane. The agent that limit activity, may be an ester of an aromatic mono - or polycarboxylic acids, such as ethyl(p-ethoxybenzoate), poly(allenglish), ester poly(alkalophiles) or an ester of fatty acids. Simple fluids may also perform a function and an additional agent that limits activity.

In one embodiment, the implementation proposed another composition of the catalyst. The catalyst composition includes one or more compositions of proletarization Ziegler-Natta. The composition of pronatalistic contains one or more transition metal compounds and an internal electron donor, which is a succinate. The composition of pronatalistic further comprises one or more of aluminium-containing socialization. The catalyst composition further comprises an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity.

In one embodiment, the implementation of the succinate I have is diethyl 2,3-diisopropylamino). The agent that determines the selectivity, can be alkoxysilane composition or simple fluids. Alkoxysilane the composition may be an n-propyltrimethoxysilane, dicyclopentadienyliron, methylcyclohexylamine or a mixture of alkoxysilanes containing n-propyltrimethoxysilane, dicyclopentadienyliron and/or methylcyclohexanecarboxylic. The agent that determines the selectivity can also be simple fluids, which may be identical or different in comparison with the previously described simple fluids, which is the internal donor, such as 2,2-dicyclopentyl-1,3-dimethoxypropane. The agent that limit activity, may be an ester of an aromatic mono - or polycarboxylic acids, such as ethyl(p-ethoxybenzoate), poly(allenglish), ester poly(alkalophiles) or an ester of fatty acids. Simple fluids may also perform a function and an additional agent that limits activity.

In one implementation, the agent that determines the selectivity, is a simple fluids, and the agent, limiting activity, is an ester of carboxylic acid. For example, an agent that determines the selectivity, can be a 2,2-dicyclopentyl-1,3-dimethoxypropane and agent, limited to the surrounding activity, can be an ester of a fatty acid. Simple fluids may also perform a function and an additional agent that limits activity.

In one embodiment, the implementation proposed another composition of the catalyst. The catalyst composition includes one or more compositions of proletarization Ziegler-Natta. The composition of pronatalistic contains one or more transition metal compounds and an internal electron donor, which is dialkoxybenzene. The composition of pronatalistic further comprises one or more of aluminium-containing socialization. The catalyst composition also contains an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity.

In one embodiment, the implementation dialkoxybenzene is 1 ethoxy-2-n-phenoxybenzoyl. The agent that determines the selectivity, can be alkoxysilane composition or amine composition. The agent that limit activity, may be an ester of an aromatic carboxylic acid or simple fluids. Simple fluids may also perform a function and an additional agent that determines the selectivity.

In one implementation, the agent that determines the selectivity performance is to place alkoxysilane composition, such as methylcyclohexylamine, and the agent, limiting activity, is an ester of carboxylic acid, such as ethyl(p-ethoxybenzoate).

In one implementation, the agent that determines the selectivity, is an amine composition, and the agent that limit activity, may be an ester of an aromatic carboxylic acid and/or simple fluids. For example, an agent that determines the selectivity, can be an amine composition, such as 2,2,6,6-tetramethylpiperidine, and the agent that limit activity, may be an ester of an aromatic carboxylic acid, such as ethyl(p-ethoxybenzoate). In an alternative embodiment, the agent that determines the selectivity, can be a 2,2,6,6-tetramethylpiperidine, and the agent that limit activity, may be a simple fluids, such as 2,2-Diisobutyl-1,3-dimethoxypropane. Simple fluids may also perform a function and an additional agent that determines the selectivity.

In one embodiment, the implementation proposed another composition of the catalyst. The catalyst composition includes one or more compositions of proletarization Ziegler-Natta. The composition of pronatalistic contains one or more transition metal compounds and an internal electron donor,which is an ester diol. Precatalysts also contains one or more of aluminium-containing socialization. The catalyst composition further comprises an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity.

In one embodiment, the implementation of the ester diol is a 2,4-pentandiol(p-n-butyl)benzoate. The agent that determines the selectivity, can be alkoxysilane the song, and the agent that limit activity, may be an ester of an aromatic carboxylic acid. For example, an agent that determines the selectivity, can be methylcyclohexylamine, and the agent that limit activity, may represent ethyl(p-ethoxybenzoate).

The presence of an external electron donor in these compositions, catalysts, opissyvayusya in this document, makes these compositions of the catalysts are self-extinguishing. Any song catalysts, vpisivaushiesya in this document may include the molar ratio between aluminum and total external electron donor in the range from 0.5:1 to 4:1. In the case of polymeric or oligomeric agents, limiting activity, the catalyst composition may include the molar ratio between aluminum and is the current electron donor in the range from 1.0:1 to 50:1.

In one embodiment, the implementation of the proposed method of polymerization. The polymerization method includes contacting, under polymerization of the olefin with the catalyst composition. The composition of the catalyst composition contains pronatalistic Ziegler-Natta containing transition metal compound and an internal electron donor. The internal electron donor is a bidentate connection, eliminating phthalates. The composition of the catalyst also contains the aluminium-containing socialization and an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity. The method further includes obtaining the polyolefin composition.

In one embodiment, the implementation of the polymerization method includes contacting propylene with a catalyst composition and education Propylenediamine polymer, characterized by a content of fraction soluble in xylene, in the range of from about 0.5% to about 10%. In one additional embodiment, the implementation of the polymerization method includes contacting propylene and ethylene with the catalyst composition and the formation of a copolymer of propylene and ethylene.

In one embodiment, the implementation of the method of polymerization involves controlled exposure at the time of conducting the polymerization reaction ratio between the quantities of aluminum and total external electron donor in the range from 0.5:1 to 4:1. In the case of polymeric or oligomeric agents, limiting activity, the composition of the catalyst may have a molar ratio between aluminium and the external electron donor in the range from 1.0:1 to 50:1.

One advantage of the present description, the invention is not contain phthalates composition of the catalyst obtain polyolefins.

One advantage of the present description of the invention is to offer an improved catalyst composition.

One advantage of the present description of the invention consists in the composition of the catalyst, which provides reception does not contain phthalates polyolefin and, in particular, does not contain phthalates polypropylene composition.

One advantage of the present description of the invention is to offer self-extinguishing composition of the catalyst, which does not contain platogo internal electron donor.

One advantage of the present description of the invention consists in the method of polymerization, characterized by reduced fouling of the reactor and reduced glomerulone polymer.

One advantage of the present description of the invention is to obtain not contain phthalates Propylenediamine polymer, characterized by high isotacticity and low-fraction content, the solution is my in xylene.

DETAILED description of the INVENTION

Any numerical range cited herein includes all values from the lower value to the upper value in increments of one unit provided that between any lower value and any of the top value, there is a separation, comprising at least two units. By way of example, you can say that the allegations hit compositional, physical or other properties, such as molecular weight, melt index, and the like, in the range from 100 to 1000, assumed to be unambiguous enumeration in this description, all individual values, such as 100, 101, 102, and the like, and sub ranges, such as 100 to 144, 155 to 170, 197 to 200, and the like. In the case of ranges that contain values that are less than one, or contain fractional numbers greater than one (for example, of 1.1, 1.5 and the like), one unit will be considered equal to 0.0001 to 0.001, 0.01 or 0.1, depending on the situation. In the case of ranges that contain single-digit numbers less than ten (for example, from 1 to 5), one generally will be considered to be equal to 0.1. These are just examples of what is implied, and expressly indicated in this application should be considered all the possible combinations, accounting for the s values between the lowest value and highest value. For example, any numerical range given in this document includes the values that are "large" or "greater or equal to the lower value. Similarly, any numerical range given in this document, includes values that are "smaller" or "less or equal to the upper value. In accordance with the discussion herein numerical ranges indicated with the reference density, the mass percentage of component, molecular weight and other properties.

The term "composition" in accordance with the use herein includes a mixture of materials, which composition contains, as well as reaction products and decomposition products formed from the materials of the composition.

The term "polymer" represents a macromolecular compound obtained by polymerization of monomers of the same or different types. "Polymer" includes homopolymers, copolymers, terpolymers, interpolymer and the like. The term "interpolymer" refers to a polymer resulting from polymerization of at least two types of monomers or comonomers. It includes the following but is not limited to: copolymers (commonly referred polymers derived from two different types of monomers or comonomers), terpolymer (usually referred to as the polymer p is obtained from three different types of monomers or comonomers), terpolymer (commonly referred polymers obtained from four different types of monomers or comonomers), and the like.

As discussed earlier, the term "interpolymer" in accordance with the usage in this document refers to a polymer resulting from polymerization of at least two different types of monomers. Thus, the generic term "interpolymer" includes copolymers, usually used to refer to polymers derived from two different types of monomers, and polymers derived from more than two different types of monomers.

The terms "blend" or "polymer blend" in accordance with the usage in this document to denote the composition of two or more polymers. This mixture may or may not be mixed. This mixture may or may not be phase-separated. This mixture according to the definition by the method of transmission electron spectroscopy may include or may not include one or more configurations of domains.

The present composition of the catalyst composition contains pronatalistic Ziegler-Natta, the internal electron donor, socialization and an external electron donor, every member of which will be discussed in detail later. In the present catalyst composition may be used any conventional sense is talization Ziegler-Natta, which is widely known at the present level of technology. In one implementation, the composition of pronatalistic Ziegler-Natta contains a compound of a transition metal compound of the metal of group 2. The transition metal compound may be a solid complex produced from the compound of the transition metal, for example, hidrocarbonetos, hidrocarburos, halides of titanium, zirconium, chromium or vanadium or mixtures thereof.

The transition metal compound described by General formula TrXxwhere Tr is a transition metal, X represents halogen or1-10hydrocarbonbearing or hydrocarbonous group, and x represents the number of such groups X in the compound in combination with a compound of the metal of group 2. Tr can be a metal of group 4, 5 or 6. In one embodiment, the implementation of the Tr is a metal of group 4, such as titanium. X can be a chloride, bromide,1-4the alkoxide or phenoxide or their mixture. In one embodiment, the realization of X is a chloride.

Non-limiting examples of suitable transition metal compounds that can be used to produce compositions of pronatalistic Ziegler-Natta represent TiCl4, ZrCl4, TiBr4, TiCl3, Ti(OC2H5)3Cl, Zr(OC2H5)3Cl, Ti(OC2H5)3Br, Ti(OC3H7)2Cl2, Ti(OC6H5)2Cl2, Zr(OC2H5)2Cl2and Ti(OC2H5)Cl3. Can also be used and mixtures of such compounds of transition metals. A number of compounds of transition metals of any restrictions do not impose up until will be present, at least one compound of the transition metal. In one embodiment, the implementation of the transition metal compound is a compound of titanium.

Non-limiting examples of suitable compounds of metals of group 2 include magnesium halides derived dialkoxybenzene, halides alkoxyamine, oxychloride magnesium derivative diallylamine and carboxylates of magnesium. In one implementation, the compound of group 2 metal is magnesium dichloride.

In one optional implementation, the composition of pronatalistic Ziegler-Natta is a mixture of titanium fragments deposited on compounds of magnesium, or otherwise produced from them. Suitable magnesium compounds include anhydrous magnesium chloride, adducts of magnesium chloride, dialkoxy or aryloxy magnesium or karboksilirovanie dialkoxy or aryloxy magnesium. In one embodiment, the implementation of the magnesium compound is a di(C1-4 )a magnesium alkoxide, such as dioxirane.

Non-limiting examples of suitable titanium fragments include alkoxides of titanium, aryloxy titanium and/or titanium halides. Compounds used to produce the compositions of pronatalistic Ziegler-Natta include one or more di(C1-4)alkoxides of magnesium, dihalogenide magnesium, alkoxylated magnesium or mixtures thereof and one or more Tetra(C1-4)alkoxides of titanium, tetrachloride titanium, (C1-4)alkoxylation titanium or mixtures thereof.

To obtain the composition of pronatalistic Ziegler-Natta can be used in the composition of the precursor, which is widely known at the present level of technology. The composition of the precursor can be obtained by chlorination of the above-mentioned mixed magnesium compounds, titanium compounds, or mixtures thereof and may include the use of one or more compounds called "clip agents, which facilitate receiving or solubilize specific compositions in the metathesis solid/solid. Non-limiting examples of suitable clip agents include trialkylborane, especially triethylborane, phenolic compounds, especially cresol, and alkoxysilane.

In one implementation, the composition of the precursor which is a mixed compound of magnesium/titanium vpisivaushiesya formula MgdTi(ORe)fXgwhere Reis failure an aliphatic or aromatic hydrocarbon radical containing from 1 to 14 carbon atoms or COR'where R' is an aliphatic or aromatic hydrocarbon radical containing from 1 to 14 carbon atoms; each group OReis identical or different; X independently represents a chlorine, bromine or iodine; d is 0.5 to 56; or is 2-4 or 3; f is in the range from 2 to 116 or from 5 to 15; and g is in the range from 0.5 to 116 or from 1 to 3. The precursor can be obtained in the controlled deposition during the removal of alcohol from their reaction mixture used for its deposition. In one implementation, the reaction medium comprises a mixture of aromatic liquids, in particular chlorinated aromatic compounds such as chlorobenzene or chlorinated toluene, alkanols, in particular ethanol, and inorganic gloriouse agent. Suitable inorganic gloriouse agents include chlorinated derivatives of silicon, aluminum and titanium, such as titanium tetrachloride or trichloride titanium, in particular titanium tetrachloride. Remove alkanol from the solution used in the chlorination, resulting in the precipitation of the solid predecessors is tenika, characterized by a desirable morphology and specific surface area. In addition, the resulting precursor is characterized by a particularly uniform particle size and resistance to coloring particles and decomposition of the resulting pronatalistic.

After the precursor is converted into solid precatalysts as a result of additional reactions (halogenation) with inorganic derivative halide, preferably a derivative of titanium halide, and the introduction of an internal electron donor. In the case of not adding more internal electron donor in the predecessor in sufficient quantity, the first may be added separately before, during or after halogenation. This technique can be repeated one or more times, optionally in the presence of additional additives or auxiliary substances, and the final solid product may be washed with an aliphatic solvent. Suitable for use in the present description of the invention is any method of obtaining, retrieving and storing of solid pronatalistic.

One suitable method of halogenation of the precursor is the reaction between the precursor at a high temperature and a halide of tetravalent titanium, optional, prisutstvie hydrocarbon or galogenovodorodov diluent. The preferred halide of tetravalent titanium is a titanium tetrachloride. Optional hydrocarbon or halogenougljovodonika solvent used in obtaining pronatalistic polymerization of olefin, preferably contains up to 12 carbon atoms, inclusive, or up to 9 carbon atoms, inclusive. Examples of hydrocarbons include pentane, octane, benzene, toluene, xylene, alkyl benzenes and decahydronaphthalene. Examples of aliphatic kalogeropoulou include methylene chloride, metropolit, chloroform, carbon tetrachloride, 1,2-dibromoethane, 1,1,2-trichloroethane, tricorcelexa, dichloromethan and tetrakhloretan. Examples of aromatic kalogeropoulou include chlorobenzene (MCB), Brabanthal, dichlorbenzene and chlorotoluene. Aliphatic halogenougljovodonika may be a compound having at least two chloride substituent, such as carbon tetrachloride or 1,1,2-trichloroethane. Aromatic halogenougljovodonika can be a chlorobenzene or o-chlorotoluene.

Halogenoalkane can be repeated one or more times, optionally with concomitant washing with an inert liquid such as an aliphatic or aromatic hydrocarbon or halogenougljovodonika between galogenirovannami and after halogenation. In addition to t the th, to remove volatile substances, in particular TiCl4not necessarily can be used one or more ekstragirovanie, including the introduction in contact with an inert liquid diluent, especially an aliphatic or aromatic hydrocarbon, in particular at elevated temperature greater than 100°C., or greater than 110°C.

In one implementation, the composition of pronatalistic Ziegler-Natta includes a solid catalyst component obtained by (i) the suspension dialkoxybenzene in an aromatic hydrocarbon that is liquid at normal temperatures, (ii) the introduction of dialkoxybenzene in contact with the titanium halide and, in addition, (iii) introducing the resulting composition a second time in contact with the titanium halide and the introduction dialkoxybenzene in contact with one of the following internal donor (discussed below) at some point during the processing of the titanium halide in position (ii).

The composition of pronatalistic Ziegler-Natta includes an internal electron donor. The internal electron donor provides control tact and selection of the size of the crystallites of the catalyst. In one embodiment, the internal electron donor is a bidentate compound. In accordance with the usage in this document "bidentate with the Association" is a molecule or compound, which have at least two oxygen-containing functional groups (in this case oxygen-containing functional groups are the same or different), and oxygen-containing functional groups separated by at least one saturated With2-C10hydrocarbon chain, with bidentate connection eliminates phthalates. Non-limiting examples of oxygen-containing functional groups suitable for bidentate compounds include oxygen, carboxylate, carbonyl, ketone, simple ester, amide, sulfoxide, sulfon, sulfonate, postit, phosphinate, phosphate, phosphonate and phosphine oxide. One or more of the carbon atoms in the C2-C10the chain can be replaced by heteroatoms of groups 14, 15 and 16. One or more atoms N in C2-C10chain can be substituted by alkyl, cycloalkyl, alkenyl, cycloalkenyl, aryl, alkylaryl, aralkyl, halogen or a functional group containing a heteroatom of group 14, 15 or 16.

Non-limiting examples of bidentate compositions suitable for use as internal electron donors include simple diesters, succinate, glutarate, dialkoxybenzene, bis(alkoxyphenyl), esters of diols, complex alkoxyalkyl esters, and any combination thereof.

In one embodiment, the implementation of internal donor elect the ones is a simple 1,3-fluids. Simple fluids may represent a derived simple dialkylamide diapir, vpisivaushiesya the following formula:

where R1to R4independently from each other represent an alkyl, aryl or aracelio group containing up to 20 carbon atoms, which optionally may contain a heteroatom of group 14, 15, 16 or 17, with the proviso that R1and R2can be a hydrogen atom. R1and R2can also be connected with the formation of a cyclic structure, such as in the case of cyclopentadiene or fluorine. Simple diakidoy ether may be linear or branched and may include one or more of the following groups: alkyl, cycloaliphatic, aryl, alcylaryl or arylalkyl radicals containing 1-18 carbon atoms, and hydrogen. Non-limiting examples of suitable derivatives of simple dialkylated diesters include dimethyl fluids, diethyl fluids, disutility fluids, metaliteracy fluids, methylbutylamine fluids, methylcyclohexylamine fluids, 2,2-dimethyl-1,3-dimethoxypropane, 2,2-diethyl-1,3-dimethoxypropane, 2,2-di-n-butyl-1,3-dimethoxypropane, 2,2-Diisobutyl-1,3-dimethoxypropane, 2-ethyl-2-n-butyl-1,3-dimethoxypropane, 2-n-propyl-2-cyclopentyl-1,3-dimethoxypropane, 2,2-dimethyl-1,3-diethoxypropane, 2-n-propyl-2-CEC is hexil-1,3-diethoxypropane, 2-(2-ethylhexyl)-1,3-dimethoxypropane, 2-isopropyl-1,3-dimethoxypropane, 2-n-butyl-1,3-dimethoxypropane, 2-sec-butyl-1,3-dimethoxypropane, 2-cyclohexyl-1,3-dimethoxypropane, 2-phenyl-1,3-diethoxypropane, 2-Cumyl-1,3-diethoxypropane, 2-(2-phenylethyl)-1,3-dimethoxypropane, 2-(2-cyclohexylethyl)-1,3-dimethoxypropane, 2-(p-chlorophenyl)-1,3-dimethoxypropane, 2-(diphenylmethyl)-1,3-dimethoxypropane, 2-(1-naphthyl)-1,3-dimethoxypropane, 2-(forfinal)-1,3-dimethoxypropane, 2-(1-decahydronaphthalene)-1,3-dimethoxypropane, 2-(p-tert-butylphenyl)-1,3-dimethoxypropane, 2,2-DICYCLOHEXYL-1,3-dimethoxypropane, 2,2-di-n-propyl-1,3-dimethoxypropane, 2-methyl-2-n-propyl-1,3-dimethoxypropane, 2-methyl-2-benzyl-1,3-dimethoxypropane, 2-methyl-2-ethyl-1,3-dimethoxypropane, 2-methyl-2-phenyl-1,3-dimethoxypropane, 2-methyl-2-cyclohexyl-1,3-dimethoxypropane, 2,2-bis(p-chlorophenyl)-1,3-dimethoxypropane, 2,2-bis(2-cyclohexylethyl)-1,3-dimethoxypropane, 2-methyl-2-isobutyl-1,3-dimethoxypropane, 2-methyl-2-(2-ethylhexyl)-1,3-dimethoxypropane, 2-methyl-2-isopropyl-1,3-dimethoxypropane, 2,2-diphenyl-1,3-dimethoxypropane, 2,2-dibenzyl-1,3-dimethoxypropane, 2,2-bis(cyclohexylmethyl)-1,3-dimethoxypropane, 2,2-Diisobutyl-1,3-diethoxypropane, 2,2-Diisobutyl-1,3-di-n-butoxypropyl, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane, 2,2-di-sec-butyl-1,3-dimethoxypropane, 2,2-di-tert-butyl-1,3-dimethoxypropane, 2,2-dineopentyl-1,3-dimethoxypropane, 2-isopropyl-2-isopentyl-1,3-dimethoxypropane, 2-FeNi is-2-benzyl-1,3-dimethoxypropane, 2-cyclohexyl-2-cyclohexylmethyl-1,3-dimethoxypropane, 2-isopropyl-2-(3,7-dimethyloctyl)-1,3-dimethoxypropane, 2,2-aminobutiramida 1,3-dimethoxypropane, 2-isopropyl-2-cyclohexylmethyl-1,3-dimethoxypropane, 2,2-Diisobutyl-1,3-dimethoxypropane, 2-isopropyl-2-cyclohexyl-1,3-dimethoxypropane, 2-isopropyl-2-cyclopentyl-1,3-dimethoxypropane, 2,2-dicyclopentyl-1,3-dimethoxypropane, 2-n-heptyl-2-n-pentyl-1,3-dimethoxypropane and 9,9-bis(methoxymethyl)fluorene. In one embodiment, the internal electron donor is a 2.2-Diisobutyl-1,3-dimethoxypropane, 2,2-DICYCLOHEXYL-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane or 9,9-bis(methoxymethyl)fluorene.

In one embodiment, the internal electron donor is a composition of succinate, opissyvayusya the following formula:

where R and R' can be identical or different, R and/or R' include one or more of the following groups: linear or branched alkyl, Alchemilla, cycloalkyl, aryl, arylalkyl or alcylaryl group, optionally containing heteroatoms. With the participation of one or both of the carbon atoms in positions 2 and 3 can be obtained from one or more ring structures. Non-limiting examples of suitable succinato include diethyl - (2,3-bis(trimethylsilyl)succinate, diethyl(2-Deut-util-3-methylsuccinate), diethyl(2-(3,3,3-cryptochromes)-3-methylsuccinate), diethyl - (2,3-bis(2-ethylbutyl)succinate, diethyl 2,3-diethyl-2-isopropylbenzene), diethyl - (2,3-aminobutiramida 2-methylsuccinate), diethyl - (2,3-DICYCLOHEXYL-2-methylsuccinate), diethyl 2,3-dibenzylamino), diethyl 2,3-diisopropylamino), diethyl - (2,3-bis(cyclohexylmethyl)succinate, diethyl - (2,3-di-tert-butylacrylate), diethyl - (2,3-diisobutylamine), diethyl 2,3-dineopentyl), diethyl 2,3-diisobutylamine), diethyl - (2,3-(1-trifloromethyl)succinate, diethyl(2-(9-fluorenyl)succinate, diethyl(2-isopropyl-3-isobutylamino), diethyl - (2-tert-butyl-3-isopropylamino), diethyl - (2-isopropyl-3-cyclohexylbenzene), diethyl(2-isopentyl-3-cyclohexylbenzene), diethyl - (2-cyclohexyl-3-cyclopentylamine), diethyl(2,2,3,3-tetramethylbenzene), diethyl - (2,2,3,3-tetramethylbenzidin), diethyl - (2,2,3,3-Tetra-n-profilaktika), diethyl - (2,3-diethyl-2,3-diisopropylamino), Diisobutyl(2,3-bis(trimethylsilyl)succinate), Diisobutyl(2-sec-butyl-3-methylsuccinate), Diisobutyl(2-(3,3,3-cryptochromes)-3-methylsuccinate), Diisobutyl(2,3-bis(2-ethylbutyl)succinate), Diisobutyl(2,3-diethyl-2-isopropylbenzene), Diisobutyl(2,3-aminobutiramida 2-methylsuccinate), Diisobutyl(2,3-DICYCLOHEXYL-2-methylsuccinate), Diisobutyl(2,3-dibenzylamino), Diisobutyl(2,3-diisopropylamino), Diisobutyl(2,3-bis(cyclohexylmethyl)succinate), Diisobutyl(2,3-di-tert-butylacrylate), Diisobutyl(2,3-shall isobutylamino), Diisobutyl(2,3-dineopentyl), Diisobutyl(2,3-diisobutylamine), Diisobutyl(2,3-bis(3,3,3-cryptochromes)succinate), Diisobutyl(2,3-di-n-profilaktika), Diisobutyl(2-(9-fluorenyl)succinate), Diisobutyl(2-isopropyl-3-isobutylamino), Diisobutyl(2-tert-butyl-3-isopropylamino), Diisobutyl(2-isopropyl-3-cyclohexylbenzene), Diisobutyl(2-isopentyl-3-cyclohexylbenzene), Diisobutyl(2-n-propyl-3-(cyclohexylmethyl)succinate), Diisobutyl(2-cyclohexyl-3-cyclopentylamine), Diisobutyl(2,2,3,3-tetramethylbenzene), Diisobutyl(2,2,3,3-tetramethylbenzidin), Diisobutyl(2,2,3,3-Tetra-n-profilaktika), Diisobutyl(2,3-diethyl-2,3-diisopropylamino), dineopentyl(2,3-bis(trimethylsilyl)succinate), dineopentyl(2,2-di-sec-butyl-3-methylsuccinate), dineopentyl(2-(3,3,3-cryptochromes)-3-methylsuccinate), dineopentyl(2,3-bis(2-ethylbutyl)succinate), dineopentyl(2,3-diethyl-2-isopropylbenzene), dineopentyl(2,3-aminobutiramida 2-methylsuccinate), dineopentyl(2,3-DICYCLOHEXYL-2-methylsuccinate), dineopentyl(2,3-dibenzylamino), dineopentyl(2,3-diisopropylamino), dineopentyl(2,3-bis(cyclohexylmethyl)succinate), dineopentyl(2,3-di-tert-butylacrylate), dineopentyl(2,3-diisobutylamine), dineopentyl(2,3-dineopentyl), dineopentyl(2,3-diisobutylamine), dineopentyl(2,3-bis(3,3,3-cryptochromes)succinate), dineopentyl(2,3-n-profilaktika), dineopentyl(2-(9-fluoren the l)succinate), dineopentyl(2-isopropyl-3-isobutylamino), dineopentyl(2-tert-butyl-3-isopropylamino), dineopentyl(2-isopropyl-3-cyclohexylbenzene), dineopentyl(2-isopentyl-3-cyclohexylbenzene), dineopentyl(2-n-propyl-3-(cyclohexylmethyl)succinate), dineopentyl(2-cyclohexyl-3-cyclopentylamine), dineopentyl(2,2,3,3-tetramethylbenzene), dineopentyl(2,2,3,3-tetramethylbenzidin), dineopentyl(2,2,3,3-Tetra-n-profilaktika), dineopentyl(2,3-diethyl-2,3-diisopropylamino), diethyl - (1,2-cyclohexanedicarboxylate) and diethyl - (norbornene-2,3, in primary forms), including stereospecific isomer (isomer) and/or a mixture of isomers of each of the above succinate. In one embodiment, the internal electron donor is a diethyl 2,3-diisopropylamino).

In one embodiment, the internal electron donor is dialkoxybenzene. Dialkoxybenzene can be a 1,2-dialkoxybenzene, vpisivaushiesya the following formula:

where R1and R2represent1-C10or2-C6alkali, which may be linear, branched or cyclic, and the number 3-6 indicate the position on the benzene ring, which optionally can be substituted.

R1and R2may be identical or different from each other. In the case in which ice branching in R 1and R2in the position of the carbon atom attached to the oxygen atom donor to the catalyst is not well attached, therefore, any steric volume created by the fork, is located, at least removing one carbon atom from the oxygen atom (for example, isopentane). Non-limiting examples of suitable alkoxygroup include propoxy, n-butoxy, n-pentox, isopentane, n-hexose, n-actoxy, 3 cyclohexylpropionic and 4 cyclopentyloxy. In one implementation, at least one alkoxygroup is ethoxy.

In positions 3-6 of the benzene ring may have substituents, for example, hydrocarbons containing less than ten carbon atoms including alkyl [e.g. methyl or tert-butyl], aryl [e.g., naphthyl], cycloaliphatic [e.g., cyclopentyl] or alkaryl), hydrocarbons containing less than ten carbon atoms (for example, alkoxy, aryloxy or alkalilike), silyl group (for example, silyl or trimethylsilyl), or halogen (such as Cl or F). In one embodiment, the implementation in the benzene ring, there is only one substitution, or does not exist at all. In one additional embodiment, implementing a single Deputy is present in position 4.

Non-limiting examples of suitable 1,2-dialkoxybenzene include 1-this is si-2-methoxy-3-methylbenzol; 1,2-diethoxybenzene, 1,2-diethoxy-3-torbenson; 1,2-diethoxy-3-methylbenzol; 1,2-diethoxy-4-tert-butylbenzoyl; 1,2-diethoxy-3-trimethylsilylmethyl; 1 ethoxy-2-n-propoxyphenol; 1,2-di-n-propoxyphenol; 1 ethoxy-2-n-phenoxybenzoyl; 1,2-desaparecimento; 1,2-dioxynaphthalene; 2,3-diethoxy-5,6,7,8-tetrahydronaphthalen; 1,2-di-n-butoxybenzoyl; 1 isobutoxy-2-ethoxy-3-fluoro-5-tert-butylbenzoyl; and 1 ethoxy-2-n-hexoxyethanol. In one implementation, dialkoxybenzene is a 1-ethoxy-2-n-phenoxybenzoyl.

In one embodiment, the internal electron donor is an ester diol, vpisivaushiesya the following formula:

where n is an integer in the range from 1 to 5. R1and R2may be identical or different, and each may be selected from hydrogen, methyl, ethyl, n-sawn, ISO-propyl, n-butilkoi, isobutylene, tert-butilkoi, allyl, phenyl or halogenfrei group. R3, R4, R5, R6, R7and R8may be identical or different, and each may be selected from hydrogen, halogen, substituted or unsubstituted hydrocarbide containing from 1 to 20 carbon atoms. Group R1-R6optionally can contain one or more heteroatoms to replace the carbon, bodoro who individually or together, while heteroatom selected from nitrogen, oxygen, sulfur, silicon, phosphorus and halogen. Group R1-R6can be connected with the formation of cyclic structures. R7and R8may be identical or different and can be linked to any carbon atom in position 2, 3, 4, 5 and 6 of the phenyl ring.

In accordance with the usage in this document "hydrocarbon" represents a linear or branched aliphatic radical, such as alkyl, alkenyl and quinil; alicyclic radical, such as cycloalkyl, cycloalkenyl; aromatic radical, such as monocyclic or polycyclic aromatic radical, and their combination, such as alkaryl or aralkyl.

In one embodiment, the implementation is not all of R1, R2, R3, R4, R5and R6represent hydrogen at the same time. At least one group of R3, R4, R5and R6may be a methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, phenyl or halogenfree. In one additional embodiment, the implementation of one of R3and R4, R5and R6accordingly represents hydrogen and the other represents methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, phenyl or halogenfree.

Neogranichena the existing examples of suitable esters of diols include 1,3-propilenglikolstearat, 2-methyl-1,3-propilenglikolstearat; 2-ethyl-1,3-propilenglikolstearat; 2-propyl-1,3-propilenglikolstearat; 2-butyl-1,3-propilenglikolstearat; 2,2-dimethyl-1,3-propilenglikolstearat; (R)-1-phenyl-1,3-propilenglikolstearat; (S)-1-phenyl-1,3-propilenglikolstearat; 1,3-diphenyl-1,3-propilenglikolstearat; 2-methyl-1,3-diphenyl-1,3-propilenglikolstearat; 2,2-dimethyl-1,3-diphenyl-1,3-propilenglikolstearat; 2-ethyl-1,3-di(tert-butyl)-1,3-propilenglikolstearat; 2-butyl-2-ethyl-1,3-propilenglikolstearat; 2,2-diethyl-1,3-propilenglikolstearat; 2-dimethoxymethyl-1,3-propilenglikolstearat; 2-methyl-2-propyl-1,3-propilenglikolstearat; 2-isoamyl-2-isopropyl-1,3-propilenglikolstearat; 2-isoamyl-2-isopropyl-1,3-propilenglikole(t-chlorobenzoate); 2-isoamyl-2-isopropyl-1,3-propilenglikole(m-chlorobenzoate); 2-isoamyl-2-isopropyl-1,3-propilenglikole(t-methoxybenzoate); 2-isoamyl-2-isopropyl-1,3-propilenglikole(p-methylbenzoate); 2,2-Diisobutyl-1,3-propilenglikolstearat; 1,3-aminobutiramida 1,3-propilenglikole(4-butylbenzoate); 2-ethyl-2-methyl-1,3-propilenglikolstearat; 2-amino-1-phenyl-1,3-propilenglikolstearat; 2,4-potentiellement; 3-methyl-2,4-potentiellement; 3-ethyl-2,4-potentiellement; 3-n-propyl-2,4-potentiellement; 3-n-butyl-2,4-potentiellement; 3,3-dimethyl-2,4-potentiellement; (2S,4S)-(+)-2,4-potentiellement; (2R,4R-(+)-2,4-potentiellement; 2,4-pentandiol(t-chlorobenzoate); 2,4-pentandiol(t-bromobenzoate); 2,4-pentandiol(p-methylbenzoate); 2,4-pentandiol(p-tert-butylbenzoate); 2,4-pentandiol(t-butylbenzoate); 2-methyl-1,3-potentiellement; 2-methyl-1,3-pentandiol(t-chlorobenzoate); 2-methyl-1,3-pentandiol(p-methylbenzoate); 2-butyl-1,3-pentandiol(p-methylbenzoate); 2-methyl-1,3-pentandiol(p-tert-butylbenzoate); 2,2-dimethyl-1,3-potentiellement; 2-ethyl-1,3-potentiellement; 2-butyl-1,3-potentiellement; 2-allyl-1,3-potentiellement; 2-methyl-1,3-potentiellement; 2-ethyl-1,3-potentiellement; 2-n-propyl-1,3-potentiellement; 2-n-butyl-1,3-potentiellement; 1,3-pentandiol(t-chlorobenzoate); 1,3-pentandiol(t-bromobenzoate); 1,3-pentandiol(p-methylbenzoate); 1,3-pentandiol(p-tert-butylbenzoate); 1,3-pentandiol(t-butylbenzoate); 2,2,4-trimethyl-1,3-potentiellement; and 3-methyl-1-trifluoromethyl-2,4-potentiellement; 2,4-pentandiol(t-formatives); and 3-butyl-3-methyl-2,4-potentiellement. In one embodiment, the implementation of the ester diol is a 2,4-pentandiol(p-n-butyl)benzoate.

The composition of pronatalistic Ziegler-Natta may also include an inert carrier material. The material of the carrier may be an inert solid substance that negatively does not alter the catalytic performance of the connection per the original metal. Non-limiting examples include metal oxides, such as alumina, and oxides of metalloids, such as silicon dioxide.

Acetalization designed for use in conjunction with the above composition pronatalistic Ziegler-Natta, is an aluminium-containing composition. Non-limiting examples of suitable aluminium-containing compositions include alyuminiiorganicheskikh compounds such as derivatives trialkylamine, dialkylaminomethyl, alkylamineacetate, dialkylaminoalkyl, alkylhalogenide, dialkylaminoalkyl and alkylaminocarbonyl containing 1-10, or 1-6 carbon atoms in each alkyl or alkoxide group. In one embodiment, the implementation of acetalization is a derivative of1-4trialkylamine, such as triethylaluminium (TEAl). The molar ratio between aluminum and titanium is in the range from 10:1 to 100:1 or 25:1 to 70:1 or 30:1 to 60:1 or 35:1 to 50:1 (or matches any value or subrange between these values). In one embodiment, the implementation of the molar ratio between aluminum and titanium is 45:1.

The catalyst composition also includes an external electron donor. In accordance with the usage in this document "external electron donor", not only is no other connection, added irrespective of the receipt of pronatalistic, and has at least one functional group that is capable of dhiravat pair of electrons on the metal atom. The external electron donor is a mixture of (i) one or more agents that determine the selectivity (AOC) and (ii) one or more agents that limits activity (AAO). In accordance with the usage in this document "the agent that determines the selectivity" is a composition that improves the stereoselectivity of the catalyst (i.e., decreases in the formed polymer, the quantity of the fraction soluble in xylene). In accordance with the use herein "agent, limiting activity" is a composition that reduces the activity of the catalyst increases the reaction temperature of polymerization is above the threshold temperature (i.e., temperature greater than about 85°C or 100°C). The agent that determines the selectivity, and/or agent, limiting activity, can provide a catalyst composition characterized by improved stereoselectivity, as well as the properties of fire extinguishing.

The agent that determines the selectivity, can be alkoxysilane composition, the amine composition or a composition of simple fluids is. Alkoxysilane composition described General formula: SiRm(OR')4-m(I), where R is independently in each case represents hydrocarbonous or amine group, optionally substituted by one or more substituents containing one or more heteroatoms of groups 14, 15, 16 or 17. R contains up to 20 atoms not counting hydrogen and halogen, R' represents a C1-20alkyl group, and m is 0, 1, 2 or 3. In one embodiment, the implementation of R represents a C6-12aryl or Uralkaliy,1-20alkyl, C3-12cycloalkyl,3-12branched alkyl or C3-12cyclic amine group, R' represents a C1-4alkyl, a m is 1 or 2. Non-limiting examples of suitable Milanovich compositions include dicyclopentadienyliron, di-tert-butyldimethylsilyl, methylcyclohexylamine, ethylcyclohexylamine, diphenylmethylsilane, diisobutyldimethoxysilane, di-n-propyltrimethoxysilane, diisobutyldimethoxysilane, isobutylmethylxanthine, di-n-butyldimethylsilyl, Cyclopentasiloxane, isopropylaminocarbonyl, n-propyltrimethoxysilane, n-propyltriethoxysilane, ethyltriethoxysilane, tetramethoxysilane, tetraethoxysilane, diethylaminoethoxy, cyclopentadienylmagnesium, bis(pyrrolidin is)dimethoxysilane, bis(perhydrosqualene)dimethoxysilane and dimethyldiethoxysilane. In one embodiment, the implementation of the silane composition may be dicyclopentadienyliron, methylcyclohexylamine, n-propyltrimethoxysilane or any combination of them. In one optional implementation alkoxysilane composition includes two or more of the above-mentioned Milanovich compositions.

In one implementation, the agent that determines the selectivity, is an amine composition. Non-limiting examples of suitable amine compositions include 2,6-substituted piperidine, such as 2,6-dimethylpiperidin and 2,2,6,6-tetramethylpiperidine, and 2,5-substituted piperidine. In one optional implementation piperidino connection is a 2,2,6,6-tetramethylpiperidine.

In one implementation, the agent that determines the selectivity, is a simple fluids. Simple fluids can be any simple fluids previously described herein. In one embodiment, the implementation of simple fluids is a 2.2-Diisobutyl-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane or 2,2-dicyclopentyl-1,3-dimethoxypropane. Thus, the internal electron donor may be a first simple fluids, and the agent that determines the selectivity, can depict ablate a second simple fluids. In one additional embodiment, the internal electron donor and the agent that determines the selectivity, are one and the same composition, i.e., the same simple fluids. Simple fluids AOC may also perform a function and an additional agent that limits activity.

In yet another variant implementation of the agent that determines the selectivity, may include at least one alkoxysilane, vpisivaushiesya herein, and one representative selected from amine and/or simple diapir, opissyvayusya in this document. In one optional implementation, the agent that determines the selectivity, is a mixture of dicyclopentadienyliron and simple diapir.

The catalyst composition also includes an agent that limits activity. The agent that limit activity, may be an ester of carboxylic acid or simple fluids, poly(allenglish), ester poly(alkalophiles) or polymeric or oligomeric compound that has more than one group of simple ether. A complex ester of carboxylic acid may be an ester of an aromatic mono - or polycarboxylic acid or an ester of aliphatic acid. Non-limiting examples of suitable aromatic carboxylic acids include1-10alkalo is s or cycloalkyl esters of aromatic monocarboxylic acids. Them suitable substituted derivatives include compounds substituted in the aromatic ring (rings)and ester group one or more substituents containing one or more heteroatoms of groups 14, 15, 16 or 17, in particular oxygen. Examples of such substituents include groups (poly)Olkiluoto ether, cycloalkyl ether, kilowog ether, Arakelova ether, alkylboron of tiefer, kilowog of tiefer, dialkylamino, diarylamino, dialkylamino and trialkylsilanes. A complex ester of aromatic carboxylic acid can be1-20hydrocarbonyl ester benzoic acid, where gidrolabilna group is unsubstituted or substituted by one or more substituents containing heteroatoms of groups 14, 15, 16 or 17, and its derivatives on the basis of simple1-20(poly)hidrocarburos ether or1-4alkylbenzoates and1-4alkylated in the ring derivative or methylbenzoate, ethylbenzoic, n-propylbenzoate, methyl-p-methoxybenzoate, methyl-p-ethoxybenzoate, ethyl-p-methoxybenzoate and ethyl-p-ethoxybenzoate. In one embodiment, the implementation of the aromatic monocarboxylic acid is an ethyl(p-ethoxybenzoate).

In one implementation, agent, limiting activity, is an ester of aliphatic acid. Ester al the factual acid can be a complex fatty acid ester, can be4-C30a complex ester of aliphatic acid, can be complex mono - or poly- (two or more) -ether, can be premazepam or branched, may be saturated or unsaturated, and any combination thereof. With4-C30esters of aliphatic acids may also be substituted by one or more substituents containing a heteroatom of group 14, 15 or 16 or 17. Non-limiting examples of suitable4-C30esters of aliphatic acids include1-20alkalemia esters of aliphatic C4-30monocarboxylic acids, With1-20alkalemia esters of aliphatic C8-20monocarboxylic acids, With1-4allyl mono - and diesters of aliphatic C4-20monocarboxylic acids and dicarboxylic acids, With1-4alkalemia esters of aliphatic C8-20monocarboxylic acids and dicarboxylic acids and C4-20alkylene or polycarboxylate derivatives With2-100(poly)glycols or ethers With2-100(poly)glycols. In one additional embodiment, the implementation4-C30aliphatic ester may be isopropylmyristate, di-n-butylbenzene, (poly)(allenglish)mono - or diacetate, (poly)(allenglish)mono - or demeritte, (poly)(allenglish)mono - or delaurenti, (poly)(allenglish)mono - or is maleinate, (poly)(allenglish)mono - or distearate, glycerite(acetate), gliterry triavir2-40aliphatic carboxylic acids and mixtures thereof.

In one embodiment, the implementation of a complex ester of aliphatic acid is an ester of fatty acids. In one embodiment, the implementation of an ester of a fatty acid is a mixture of esters of poly(ethylene glycol). In yet another variant implementation of an ester of a fatty acid is a mixture of esters of poly(ethylene glycol), commercially available as S-191 in the company Chem Service, Inc., West Chester, Pennsylvania.

In one implementation, agent, limiting activity, is a simple fluids. As an agent, limiting activity, can be used any simple fluids, the previously discussed herein. In one implementation, agent, limiting activity, is a 2.2-Diisobutyl-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane or texture. Simple fluids may also perform a function and an additional agent that determines the selectivity.

The composition of the catalyst may include any of the above internal electron donor (bidentate compounds) in combination with any of the external electron donor, opissyvayusya in this document. In one var is ante implementation of the present description of the invention provides a catalyst composition, containing one or more compositions of proletarization Ziegler-Natta together with one or more transition metal compounds. The catalyst composition also includes an internal electron donor, which is a simple fluids. The catalyst composition also includes one or more of aluminium-containing socialization. The catalyst composition additionally includes an external electron donor, which is a mixture of the agent that determines the selectivity, (AOC) and the agent that limits activity (antioxidant activity).

The internal electron donor may be any previously discussed simple fluids. In one embodiment, the implementation of simple fluids is a 2.2-Diisobutyl-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane, 2,2-dicyclopentyl-1,3-dimethoxypropane or 9,9-bis(methoxymethyl)fluorene. The internal electron donor may be one or any combination of data simple diesters.

The external electron donor may be a mixture of any agent that determines the selectivity, and any agent, limiting activity, opissyvayusya in this document. In one implementation, the agent that determines the selectivity represents discussed earlier alkoxysilane composition or simple fluids. In one complements the linen implementation agent, determines the selectivity, is dicyclopentadienyliron or methylcyclohexanecarboxylic. In yet another additional embodiment, the implementation of the agent that determines the selectivity represents 2,2-dicyclopentyl-1,3-dimethoxypropane. In one additional embodiment, the external electron donor can be any of the data alkoxysilanes songs or simple fluids in combination with a complex ester of an aromatic mono - or polycarboxylic acids, such as ethyl(p-ethoxybenzoate).

The present description of the invention offers another composition of the catalyst. In one implementation, the catalyst composition includes one or more compositions of proletarization Ziegler-Natta together with one or more transition metal compounds. The catalyst composition also includes an internal electron donor, which is a succinate. In the catalyst composition also includes one or more of aluminium-containing socialization. The catalyst composition additionally includes an external electron donor, which is a mixture of the agent that determines the selectivity, (AOC) and the agent that limits activity (antioxidant activity).

The internal electron donor may be any succinate, vpisivaushiesya present on the document. One non-limiting example of a suitable succinate is a diethyl 2,3-diisopropylamino).

The external electron donor may be a mixture of any agent that determines the selectivity, and any agent, limiting activity, opissyvayusya in this document. In one implementation, the agent that determines the selectivity represents discussed earlier alkoxysilane composition or simple fluids. In one optional implementation, the agent that determines the selectivity, is an n-propyltrimethoxysilane, dicyclopentadienyliron or methylcyclohexanecarboxylic. In yet another additional embodiment, the implementation of the agent that determines the selectivity, is methylcyclohexylamine, and the agent, limiting activity, represents ethyl(p-ethoxybenzoate).

In one implementation, the agent that determines the selectivity, is a simple fluids, and the agent, limiting activity, is an ester of carboxylic acid. For example, an agent that determines the selectivity, can be a 2,2-dicyclopentyl-1,3-dimethoxypropane, and the agent that limit activity, may be an ester of a fatty acid, such as S-191, which is commercially available in the company Chem Service, Inc. West Chester, Pennsylvania.

The present description of the invention offers another composition of the catalyst. In one implementation, the catalyst composition includes one or more compositions of proletarization Ziegler-Natta together with one or more transition metal compounds. The catalyst composition also includes an internal electron donor, which is dialkoxybenzene. In the catalyst composition also includes one or more of aluminium-containing socialization. The catalyst composition additionally includes an external electron donor, which is a mixture of the agent that determines the selectivity, (AOC) and the agent that limits activity (antioxidant activity).

Dialkoxybenzene can be any dialkoxybenzene, vpisivaushiesya in this document. One non-limiting example of dialkoxybenzene, suitable for use as an internal electron donor, is a 1-ethoxy-2-n-phenoxybenzoyl.

The external electron donor may be a mixture of any agent that determines the selectivity, and any agent, limiting activity, opissyvayusya in this document. In one implementation, the agent that determines the selectivity represents discussed earlier alkoxysilane composition or amine compositions is the Oia. Agent, limiting activity, represents discussed earlier ester carboxylic acids or simple fluids.

In one embodiment, the external electron donor includes alkoxysilane composition and an ester of carboxylic acid. In one optional implementation, the agent that determines the selectivity, is dicyclopentadienyliron or methylcyclohexanecarboxylic. In yet another additional embodiment, the implementation of the agent that determines the selectivity, is methylcyclohexylamine, and the agent, limiting activity, represents ethyl(p-ethoxybenzoate).

In one implementation, the agent that determines the selectivity, is an amine composition, and the agent, limiting activity, is an aromatic carboxylic acid or simple fluids. For example, an agent that determines the selectivity, can be a 2,2,6,6-tetramethylpiperidine, and the agent, limiting activity, can be a 2.2-Diisobutyl-1,3-dimethoxypropane. Simple fluids may also perform a function and an additional agent that determines the selectivity. In an alternative embodiment, the agent that determines the selectivity, can be a 2,2,6,6-tetramethylpiperidine, and the agent, limiting activity, moretraditional an ethyl(p-ethoxybenzoate).

The present description of the invention offers another composition of the catalyst. In one implementation, the catalyst composition includes one or more compositions of proletarization Ziegler-Natta together with one or more transition metal compounds. The catalyst composition also includes an internal electron donor, which is an ester diol. In the catalyst composition also includes one or more of aluminium-containing socialization. The catalyst composition additionally includes an external electron donor, which is a mixture of the agent that determines the selectivity, (AOC) and the agent that limits activity (antioxidant activity).

Ester diol can be any complex ether diol, vpisivaushiesya in this document. One non-limiting example of ester diol, suitable for use as an internal electron donor, is a 2,4-pentandiol(p-n-butyl)benzoate.

The external electron donor may be a mixture of any agent that determines the selectivity, and any agent, limiting activity, opissyvayusya in this document. In one implementation, the agent that determines the selectivity, is alkoxysilane composition. Agent, limiting the activity of t is possessing an ester of carboxylic acid.

In one implementation, the agent that determines the selectivity, is dicyclopentadienyliron or methylcyclohexanecarboxylic. In one optional implementation, the agent that determines the selectivity, is methylcyclohexylamine, and the agent, limiting activity, represents ethyl(p-ethoxybenzoate).

In any of the above compositions of the catalysts, the molar ratio between aluminum and total external electron donor may be in the range from 0.25:1 to 20:1 (or to match any value or subrange between these values) or from 0.5:1 to 4:1 or from 1:1 to 3:1 or from 2:1 to 3:1, or be less than or equal to 2.5:1. In accordance with the usage in this document "total external electron donor" is a combined number of the agent that determines the selectivity, and the agent, limiting the activity present in the composition of external electron donor. In the case of polymeric or oligomeric agents, limiting activity, the catalyst composition may include the molar ratio between aluminium and the external electron donor in the range from 1.0:1 to 50:1, (or corresponding to any value or subrange between these values). In one variant of the implementation of the molar ratio between aluminum and total external electron donor is 3:1.

As to my surprise suddenly discovered applicants neimagazine system catalysts with bidentate internal electron donor, such as simple fluids, succinate, alkoxybenzyl and/or ester diol can be converted into a self-extinguishing compositions of the catalysts resulting from the use of any of the above-mentioned external electron donor. In addition, as to his astonishment applicants, controlled by keeping the total molar ratio between aluminium and the external electron donor in the range from 0.5:1 to 4:1 best way yields a system of catalyst, which is characterized by high productivity with excellent ease of use and is self-extinguishing. In accordance with the use herein of "self-extinguishing" a catalyst is a catalyst which shows reduced activity: (1) at a temperature greater than approximately 100°C, in comparison to the activity observed under normal conditions of polymerization, or (2) at a temperature greater than 85°C, in comparison to the activity observed in the case of replacement of an agent that limits activity (AAO) with the same molar amount of an agent that determines the selectivity, (AOC). In addition, in order practical standard m who should say what what if the polymerization process, in particular gas-phase polymerization in the fluidized bed, implemented under normal conditions of processing, can be interrupted with the resulting collapse of the layer without the occurrence of adverse effects in respect of agglomerating the polymer particles, the composition of the catalyst is considered to be "self-extinguishing".

In order standardized measures polymerization activity at elevated temperatures used in this document, the catalyst activity regulate to compensate for differences in the concentrations of monomer due to temperature. For example, in the case of conditions of the liquid phase (suspension or solution) polymerization will include a correction factor to account for the reduced solubility of propylene in the reaction mixture at elevated temperatures. That is, the catalyst activity "normalize" to compensate for the reduced solubility in comparison with what takes place at low temperature, especially when the standard is 67°C. the "Normalized" activity at the temperature T or aTdefined as the measured activity or the amount (mass of polymer/weight of catalyst/hour) at a temperature T activity (T) multiplied by a correction factor for the concentration of [P(67)]/[P(T)], where [P 67] represents the concentration of propylene at 67°C, and [P(T)] represents the concentration of propylene at a temperature T. the Equation for the normalized activity is presented below:

N about p m and l and C about in and n n and I and K t and in n about with a t b ( And T ) = [ P ( 67 ) ] [ P ( T ) ] × and K t and in n about with a t b ( T )

In equation activity when the temperature T is multiplied by the ratio between the concentration of propylene at 67°C and the concentration popeline at temperature T. the Resulting normalized activity (A), adjusted to account for the reduction in the concentration of propylene with increasing temperature, can be used to map the activity of the catalyst under varying temperature conditions. Correction factors for terms used in liquid-phase polymerization, measured and brought forth.

67°C 85°C 100°C 115°C 130°C 145°C
1,00 1,42 1,93 2,39 2,98 3,70

As suggested correction factor activity during polymerization increases linearly with increasing concentration of propylene in the used conditions. The correction factor depends on the used solvent or diluent. For example, the correction factors listed previously, are common With6-10aliphatic hydrocarbon mixture (Isopar™E, available at Exxon Chemical Company). In terms of conducting the gas-phase polymerization, the solubility of the monomer is usually not important, and in General to account for temperature differences activity is not correct. That is, the activity and the normalized activity will constitute one and the same.

"The ratio of normalized activities" is defined as AT/A67where aTrepresents the activity at the temperature T, and A67represents activity at 67°C. This value can be used as an indicator and the changes of activity depending on the temperature. For example, as demonstrated by the magnitude And100/A670.30 , the activity of the catalyst at 100°C is only 30 percent of the catalyst activity at 67°C. As determined at 100°C the ratio a/a67equal to 35% or less, and usually provides the receiving system of the catalyst, which is self-extinguishing system.

In any of the above variants of realization of the external electron donor may include from about 50 mole percent to about 99 mol% (or any value or subrange between data values) of the AOA and from about 1 molar percent to about 50 mol% (or any value or subrange between these values) AOC. In the case of polymeric or oligomeric agent, limiting activity, (such as poly(allenglish) and/or an ester of poly(alkalophiles)) the external electron donor may include from about 5 mole percent to about 90 mole percent (or any value or subrange between data values) of the AOA and from about 10 mole percent to about 95 mole percent (or any value or subrange between these values) AOC.

The molar ratio between aluminium and the AOC may, at ditsa in the range from 750:1 to 1.25:1 (or to make any value in between these values) or from 150:1 to 1.25:1 or 80:1 to 1.5:1 or 40:1 to 1.67:1, or from 20:1 to 2.5:1 or 13:1 to 5:1.

The molar ratio between aluminium and the AOA can be in the range from 20:1 to 0.5:1 (or to make any value in between these values) or 6.7:1 to 0.5:1, or from 5.7:1 to 0.52:1 or from 5:1 to 0.62:1, or from 4.4:1 to 0,71:1 or from 5.3:1 to 0.5:1. The molar ratio between the external electron donor and the titanium can be in the range from about 5:1 to about 100:1. In one embodiment, the implementation of the molar ratio between the total external electron donor and the titanium is 30:1. If the content of the polymeric or oligomeric agents, limiting activity, (such as poly(allenglish) and/or an ester of poly(alkalophiles)) the molar ratio between aluminium and the AOA can be in the range from 200:1 to 1:1 (or to make any value in between these values) or from 70:1 to 1:1 or 50:1 to 1.5:1 or 30:1 to 2:1 or 20:1 to 2.5:1 or 17:1 to 3:1. The molar ratio between the total external electron donor and the titanium can be in the range from about 2:1 to about 100:1.

The present composition of the catalysts produce polypropylene composition, which is characterized by high rigidity and high isotacticity (i.e., low content of fraction soluble in xylene). As you can imagine without the desire to link sabakami any particular theory, the molar ratio between aluminium and the external electron donor in the results of the composition of the catalyst, which reproduces the property of fire extinguishing catalysts of the third generation, which as electron donor used esters of benzoic acid, without giving the resulting polymer a strong smell of benzoates. In addition, the activity of the present compositions of the catalysts with the activity of conventional catalysts fourth generation or exceed her without the use of internal electron donor on phthalates basis. Thus, the present compositions of the catalysts are showing signs of fire extinguishing catalysts third generation while meeting or exceeding the activity of the catalysts of the fourth generation.

In one embodiment, the implementation of the proposed method of polymerization. The polymerization method includes the introduction in the conditions of the polymerization of the olefin into contact with the catalyst composition. The composition of the catalyst can be any catalyst composition, opisyvayuschaya in this document, and includes the composition of pronatalistic Ziegler-Natta containing transition metal compound and an internal electron donor. The internal electron donor may be any bident is the can connection, vpisivaushiesya in this document. The catalyst composition also comprises of aluminium-containing socialization and an external electron donor. The external electron donor is a mixture of the agent that determines the selectivity, and the agent that limits activity. The method further includes obtaining the polyolefin composition.

In accordance with the usage in this document "conditions for polymerization are the parameters of temperature and pressure in the polymerization reactor, suitable for promotion of polymerization and/or copolymerization between one or more olefins and a catalyst composition to produce the desired polymer. The polymerization method may be implemented in any mode, including the method of polymerization in the gas phase, slurry or bulk, the polymerization is carried out in one or more reactors (reactor). The olefin can be1-C4alpha-olefin, including such non-limiting examples as ethylene, propylene, butene and mixtures of these olefins. The olefin may be used either in the gas state or liquid state.

In one embodiment, the implementation of the proposed method of polymerization. The polymerization method includes the introduction of propylene in contact with a catalyst composition in a polymerization reactor is. The composition of the catalyst can be any of the aforementioned compositions of the catalysts. The internal electron donor is any of the bidentate compounds discussed in this document.

In one embodiment, the implementation of the method of polymerization may include stage terpolymerization. Terpolymerization includes the introduction of a small amount of the olefin into contact with a composition of pronatalistic after administration of the composition of pronatalistic in contact with socialization and agent, determining the selectivity and/or agent, restricting activity. After that, the resulting stream is pre-activated catalyst fed to the reaction zone of the polymerization and enter into contact with the remainder of the polymerized olefin monomer and optionally one or more external electron-donor components. Terpolymerization in the results of the composition of pronatalistic combined with socialization and agent, determining the selectivity and/or agent, limiting activity, when this combination is dispersed in the matrix of the resulting polymer. Optional can be added an additional amount of the agent that determines the selectivity, and/or agent, restricting activity.

In one embodiment, the implementation of the method of polymerization viewlocity preliminary activation. Preliminary activating includes the introduction of the composition of pronatalistic in contact with socialization and agent, determining the selectivity and/or agent, restricting activity. After that, the resulting stream is pre-activated catalyst fed to the reaction zone of the polymerization and enter in contact with the polymerized olefin monomer and optionally one or more external electron-donor components. Pre-activation results in obtaining the composition of pronatalistic combined with socialization and agent, determining the selectivity and/or agent, restricting activity. Optional can be added an additional amount of the agent that determines the selectivity, and/or agent, restricting activity.

In one implementation, the method includes maintaining or controlled by keeping the molar ratio between aluminum and total external electron donor in the range from about 0.5:1 to about 4:1. In other words, the ratio of aluminum and total external electron donor regulate during the entire polymerization process, supporting or controlled by maintaining this ratio in the range from 0.5:1 to 4:1 or from 1:1 to 3:1 or 3:1. How is olymerization further includes receiving Propylenediamine polymer. Thus, the ratio of aluminum and an external electron donor controlled withstand the regulation number of external electron-donor component introduced into the reaction, while maintaining a constant number of aluminum or the throttling of aluminum while maintaining the amount of external donor or resulting from the use of a combination of both methods. In the case of polymeric or oligomeric agents, limiting activity, the catalyst composition may include the molar ratio between aluminium and the external electron donor in the range from 1.0:1 to 50:1.

In one embodiment, the implementation of the method of polymerization may also include the maintenance, regulation or other controlled keeping the ratio between the amounts of aluminum and titanium at a level of approximately 45:1.

In one embodiment, the implementation of the polymerization method includes the introduction of propylene in contact with the catalyst composition and obtaining Propylenediamine polymer. Propylenediamine polymer obtained by the polymerization method may be a polypropylene homopolymer or copolymer of propylene and one or more comonomers. Comonomer can be an alpha-olefin containing 2 to 12 carbon atoms. Neoprene ewusie examples of suitable comonomers include ethylene, 1-butene, 1-hexene, 4-methylpentene, 1-hepten and 1-octene. Therefore, the polypropylene composition may be a polypropylene homopolymer or a propylene polymer monomer and one or more comonomers. In one embodiment, the implementation Propylenediamine polymer is characterized by a content of fraction soluble in xylene, in the range from approximately 0.5% to approximately 10.0% when calculating the weight, or from about 2.0% to about 5.0 percent when calculating the masses.

In one embodiment, the implementation of the method of polymerization includes the damping composition of the catalyst or the polymerization reaction at excess temperature in the polymerization reactor to approximately 100°C.

In one embodiment, the implementation of the method of polymerization is a method of gas-phase polymerization, implemented in one or more than one reactor. A suitable gas-phase polymerization involves the use of mode of condensation, as well as the mode of sverkajuschii when gas components, including added inert low-boiling compounds in the reactor is pumped in liquid form to the heat sink. In the case of multiple reactors is desirable functioning of a series connection, that is, the product stream from the first reactor was loaded in the second react the R, and to continue the polymerization add a further quantity of monomer or other monomer. Can be added an additional amount of catalyst or catalyst components (i.e., pronatalistic or socializaton), as well as an additional amount of a mixture of external electron donors, the other a mixture of external electron donor or an individual alkoxysilane and/or one or more agents that limit activity.

The polymerization method may include the introduction of propylene and ethylene in contact with the catalyst composition and obtaining a copolymer of propylene and ethylene. In one embodiment, the implementation of the method of polymerization is realized in two reactors in which to obtain the copolymer in contact impose two olefin, such as propylene and ethylene. In the first reactor receive polypropylene, and the second reactor in the presence of polypropylene from the first reactor to obtain a copolymer of ethylene and propylene. Regardless of the used methods of polymerization it is necessary to understand that its external electron donor, precatalysts and/or socialization can be introduced into the contact before adding to the reactor and in the absence of other components of the polymerization, in particular the monomer. In one embodiment, the implementation of the above dual methods of polymerization are the mortar is cured.

The temperature of the polymerization reactor is in the range from 40 to 130°C. or from 60 to 100°C or 65°C to 80°C. the Above temperatures are average temperatures of the reaction mixture measured at the walls of the reactor. Isolated region of the reactor may be exposed to localized temperatures that exceed the above limits.

In order to bring the example, and not limitation, will be further examples of the present description of the invention.

EXAMPLES

(1) preparation of catalyst

Catalyst A:The catalyst was prepared in an atmosphere of N2in accordance with the following methodology: (1) 12.00 g of MagTi precursor (obtained as described in example 1 of document US6825146) enter into contact with 175 ml of TiCl4in MHB (1:1 (by vol.:vol.), and then from 4.80 ml 1 ethoxy-2-n-phenoxybenzene (industrial safety examinations). The mixture is heated to 100°C and maintained at this temperature for 60 minutes, followed by filtration to remove solvent. This technique was repeated twice. (2) the Resulting solid is washed 3 times using 200 ml of isooctane at 25°C, followed by filtration. Then the solid is dried in a stream of N2. Analysis by the method of x-ray fluorescence shows the content in the solid catalyst of 4.45% (wt is.) Ti.

The catalyst:(1) In a flask in an atmosphere of N2download 12.00 g of MagTi precursor and 2.46 g of 9,9-bis(methoxymethyl)fluorene (BMFI). Add 175 ml of TiCl4in MHB (1:1 (by vol.:vol.)). The mixture is heated to 115°C. and maintained at this temperature for 60 minutes, followed by filtration to remove solvent. (2) To solid substance add 175 ml of TiCl4in MHB (1:1 (by vol.:vol.), the mixture for 30 minutes, maintained at 115°C and then filtered. This technique is repeated once. (3) the Resulting solid is washed 3 times using 200 ml of isooctane at 25°C, followed by filtration. Then the solid is dried in a stream of N2. Analysis by the method of x-ray fluorescence shows the content in the solid catalyst 4.32 percent (mass.) Ti.

The catalyst With:(1) 12.00 g of MagTi precursor is introduced into contact with 175 ml of TiCl4in MHB (1:1 (by vol.:vol.), and then 2,40 ml of 2,2-Diisobutyl-1,3-dimethoxypropane (DiBMP). The mixture is heated to 115°C. and maintained at this temperature for 60 minutes, followed by filtration to remove solvent. (2) To solid substance add 175 ml of TiCl4in MHB (1:1 (by vol.:vol.), the mixture for 30 minutes, maintained at 115°C and then filtered. This technique is repeated once. (3) Resulting from the solid substance is washed 3 times using 200 ml of isooctane at 25°C, followed by filtration. Then the solid is dried in a stream of N2. Analysis by the method of x-ray fluorescence shows the content in the solid catalyst 3,59% (mass.) Ti.

The catalyst D:Same as catalyst C, except instead of 2.40 ml of 2,2-Diisobutyl-1,3-dimethoxypropane 2,48 ml of diethyl - (2,3-diisopropylamino). The content of Ti is 3.75% (mass.).

Catalyst E:Same as catalyst C, except (1) instead of 2.40 ml of 2,2-Diisobutyl-1,3-dimethoxypropane 2,88 ml 2,4-pentadione(p-n-butyl)benzoate and (2) using 200 ml of a solution of TiCl4instead of 175 ml at each injection in contact with TiCl4. The content of Ti is to 3.92% (mass.).

The catalyst F:(1) 3.00 g of MagTi precursor is introduced into contact with 60 ml of a solution of TiCl4in MHB (1:1 (by vol.:vol.), and then 0.42 ml of 2,2-dicyclopentyl-1,3-dimethoxypropane. The mixture is heated to 115°C. and maintained at this temperature for 60 minutes, followed by filtration to remove solvent. (2) To the solid substance was added 60 ml of a solution of TiCl4in MHB (1:1 (by vol.:vol.), the mixture for 30 minutes, maintained at 115°C and then filtered. This technique is repeated once. (3) the Resulting solid is washed 3 times using 70 ml of isooctane at 25°C, followed by filtration. the donkey this solid is dried in a stream of N 2. Analysis by the method of x-ray fluorescence shows the content in the solid catalyst 4,79% (mass.) Ti.

The catalyst G:Same as catalyst F, except for adding to the reaction mixture during the second injection into contact with TiCl40,42 ml of 2,2-dicyclopentyl-1,3-dimethoxypropane. The content of Ti in the solid catalyst is 2,81% (mass.).

(2) Polymerization

The particle size of the powdered catalyst reduced in the mixing anchor magnetic stirrer solid catalyst within 30-45 minutes. After that, the toluene receive a suspension of the catalyst. The concentration of suspensions and load for each catalyst are shown next.

Catalyst Ti, wt.% The suspension concentration, µg/ml Loading, μg/reactor
And of 4.45 144 39,5
In 4,32 148 40,7
3,59 178 D 3,75 170 46,9
E 3,92 163 44,8
F 4,79 213 58,6
G 2,81 232 63,9

All AOC and the AOA is diluted to a concentration of 0.005 M in solvent Isopar E™ except product S-191, which before feeding into the system Parallel Polymerization Reactors (PPRs from Symyx Technologies, Inc.) dissolved in toluene. For solvent Isopar E™ receive TEAl (triethylaluminum), which is used in the form of solutions with concentrations of 0.02 or or 0,1 M

Purged the reactor PPR heated to 50°C., in each reactor add TEAl and make-up solvent Isopar E™, followed by addition of N2to achieve a stable pressure of 0.34 MPa. The reactor is heated to the desired temperature (67, 100, or 115°C). Add propylene to 6.80 ATM and within 10 minutes have stabilized. In each reactor type AOC or a mixture of EPA and the AOA and 500 μl of acceptor unreacted substances in the solvent Isopar E™ directly following the m further addition of catalyst (275 μl) and 500 μl of acceptor unreacted substances in the solvent Isopar E™. Reaction quenched WITH2after 60 minutes or when the maximum relative degree of conversion of 100.

(3) measurement of the value XS

The percent soluble in xylene fraction (% XS) in polypropylene (PP) is a property of the material listed in multiple tables with the specifications of the products and methods of measurement set out in document ASTM method D 5492-98. In the method determine the fraction of PP sample, which is soluble in o-xylene at 25°C. the Soluble fraction shows good correlation with the percentage of amorphous fractions in PP. The content of the amorphous fraction is closely related to the operational characteristics of the final product, and is a critical factor for process control. To measure the % fraction of polypropylene (PP), soluble in trichlorobenzene, (% TCB) and establish a correlation between this value and % fraction soluble in xylene, standards-based PP use the tool fixture. The structure of the system is based on the working area of the liquid manipulator Cavro and mounted in the housing together with peripherals, custom-made for handling hot polymer solutions, sealing, filtering and analysis. The robotic system Cavro and infrared detector on the basis of the Polymer Char IR4 filter, used for determination of the concentration of polymer solution through an interface associated with a personal computer. The versatility of the device makes possible its use in standalone mode for the dilution of the polymer samples and the creation of duplicate samples. Forty-nine samples can be processed within 10 hours, which corresponds to the increase in ~10X in comparison with what occurs to such methods ASTM a transaction manually, using only 30 mg in comparison with a standard sample 2, In the General case of diluted samples during the analysis of the heated and maintained at 160°C, then the individual images are transferred in the unit of measurement, which heats the sample up to 175°C for analysis by using the infrared detector IR4. After analysis of all the samples in the block of samples within 1 hour, cooled to 40°C, hold filtration, heated to 60°C for the preservation of the remaining polypropylene in solution, and then repeated the analysis at 175°C using IR4. The difference in readings before and after is the basis for the final value % TCB (% XS). The fraction soluble in TCB, measured only for cells that generate sufficient amount of polymer.

As shown by the data in table 1, the activity of the catalyst at an elevated temperature such as 100°C and 115°C, will be significantly reduced in case of replacement of part of the AOC on the AOA, while maintaining high activity and stereoselectivity of the catalyst.

For the purposes of patent practice in the United States the contents of any patent, patent applications and publications cited herein in its entirety by reference is incorporated herein, in particular in the description of the structures, methods of synthesis and a General idea of the modern state of the art. You must understand that experts in the relevant field of technology should be obvious, and various changes and modifications of the preferred in the present implementation options, opissyvayusya in this document. Such changes and modifications can be obtained without deviating from the scope and essence of the present description of the invention and without limiting its intended benefits. Therefore provides for the inclusion of such changes and modifications in the appended claims.

1. The composition of the catalyst containing:
one or more compositions of proletarization Ziegler-Natta containing one or more transition metal compounds and an internal donor elect the ones, containing bidentate compound having at least two oxygen-containing functional groups, which are separated by at least one saturated With2-C10hydrocarbon chain;
one or more of aluminium-containing socialization; and an external electron donor containing a mixture of the agent that determines the selectivity selected from the group consisting of alkoxysilane composition and simple diapir, and agent, limiting activity, selected from the group consisting of a complex ester of an aromatic mono - or polycarboxylic acid and a complex ester of fatty acid.

2. The composition of the catalyst according to claim 1, where the bidentate compound selected from the group consisting of simple diapir, succinate, glutarate, complex ether diol and combinations thereof.

3. The composition of the catalyst according to claim 2, where the bidentate compound contains simple fluids.

4. The composition of the catalyst according to claim 3, where simple fluids are selected from the group consisting of 2,2-Diisobutyl-1,3-dimethoxypropane, 2-isobutyl-2-isopropyl-1,3-dimethoxypropane, 2,2-dicyclopentyl-1,3-dimethoxypropane and 9,9-bis(methoxymethyl)fluorene.

5. The composition of the catalyst according to claim 3, where the agent that determines the selectivity, which are selected from the group consisting of n-propyltrimethoxysilane, dicyclopentadienyliron, methylcyclohexylamine and their combination is s.

6. The composition of the catalyst according to claim 3, where the agent that determines the selectivity represents 2,2-dicyclopentyl-1,3-dimethoxypropane.

7. The composition of the catalyst according to claim 3, where the agent, limiting activity, selected from the group consisting of ethyl(p-ethoxybenzoate) and esters of fatty acids.

8. The composition of the catalyst according to claim 2, where the internal electron donor contains succinate.

9. The composition of the catalyst according to claim 1, where succinate is diethyl 2,3-diisopropylamino).

10. The catalyst composition of claim 8, where the external electron donor includes 2,2-dicyclopentyl-1,3-dimethoxypropane and an ester of a fatty acid.

 

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