Olefin polymerization catalyst system comprising mesoporous organosilica support
First Claim
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1. A catalyst system comprising:
- one or more olefin polymerization catalyst compounds;
a catalyst support comprising an organosilica material that is a polymer of at least one monomer of Formula [Z1OZ2SiCH2]3 (I), wherein Z1 represents a hydrogen atom, a C1-C4 alkyl group, or a bond to a silicon atom of another monomer and Z2 represents a hydroxyl group, a C1-C4 alkoxy group, a C1-C6 alkyl group, or an oxygen atom bonded to a silicon atom of another monomer; and
an activator.
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Abstract
A catalyst system comprising a combination of: 1) an activator; 2) one or more metallocene catalyst compounds; 3) a support comprising an organosilica material, which may be a mesoporous organosilica material. The organosilica material may be a polymer of at least one monomer of Formula [Z1OZ2SiCH2]3 (I), where Z1 represents a hydrogen atom, a C1-C4 alkyl group, or a bond to a silicon atom of another monomer and Z2 represents a hydroxyl group, a C1-C4 alkoxy group, a C1-C6 alkyl group, or an oxygen atom bonded to a silicon atom of another monomer. This invention further relates to processes to polymerize olefins comprising contacting one or more olefins with the above catalyst system.
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Citations
21 Claims
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1. A catalyst system comprising:
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one or more olefin polymerization catalyst compounds; a catalyst support comprising an organosilica material that is a polymer of at least one monomer of Formula [Z1OZ2SiCH2]3 (I), wherein Z1 represents a hydrogen atom, a C1-C4 alkyl group, or a bond to a silicon atom of another monomer and Z2 represents a hydroxyl group, a C1-C4 alkoxy group, a C1-C6 alkyl group, or an oxygen atom bonded to a silicon atom of another monomer; and an activator. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21)
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2. The catalyst system of claim 1, wherein olefin polymerization catalyst compound is a coordination polymerization catalyst compound.
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3. The catalyst system of claim 1, wherein Z2 represents a hydroxyl group, a C1-C4 alkoxy group, or an oxygen atom bonded to a silicon atom of another monomer, and, optionally, Z1 represents a hydrogen atom, methyl, ethyl or a bond to a silicon atom of another monomer.
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4. The catalyst system of claim 1, wherein the polymer further comprises a second distinct monomer of Formula [Z1OZ2SiCH2]3 (I).
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5. The catalyst system of claim 1, wherein the organosilica material further comprises at least one monomer selected from the group consisting of:
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a monomer of Formula Z3OZ4Z5Z6Si (II), wherein Z3 represents a hydrogen atom or a C1-C4 alkyl group, or a bond to a silicon atom of another monomer; and
Z4, Z5 and Z6 are each independently selected from the group consisting of a hydroxyl group, a C1-C4 alkyl group, a C1-C4 alkoxy group, a nitrogen-containing C1-C10 alkyl group, a nitrogen-containing heteroaralkyl group, a nitrogen-containing optionally substituted heterocycloalkyl group, and an oxygen atom bonded to a silicon atom of another monomer;a monomer of Formula Z7Z8Z9Si—
R1—
SiZ7Z8Z9 (III), wherein Z7 represents a hydroxyl group, a C1-C4 alkoxy group, or an oxygen atom bonded to a silicon atom of another monomer;
Z8 and Z9 each independently represent a hydroxyl group, a C1-C4 alkoxy group, a C1-C4 alkyl group, or an oxygen bonded to a silicon atom of another monomer; and
R1 is selected from the group consisting of a C1-C8 alkylene group, a C2-C8 alkenylene group, a C2-C8 alkynylene group, a nitrogen-containing C2-C10 alkylene group, an optionally substituted C6-C20 aralkylene and an optionally substituted C4-C20 heterocycloalkylene group;a trivalent metal oxide monomer of Formula M1(OZ10)3 (IV), wherein M1 represents a Group 13 metal and Z10 represents a hydrogen atom, a C1-C6 alkyl or a bond to a silicon atom of another monomer; a trivalent metal oxide monomer of Formula (Z11O)2M2-O—
Si(OZ12)3 (V), wherein M2 represents a Group 13 metal and Z11 and Z12 each independently represent a hydrogen atom, a C1-C6 alkyl group, or a bond to a silicon atom of another monomer;a cyclic polyurea monomer of Formula
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6. The catalyst system of claim 1, wherein the catalyst support comprising an organosilica material has:
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an average pore diameter between about 2 nm and about 50 nm; a pore volume about 0.1 cm3/g to about 10 cm3/g; and
/ora surface area of about 100 m2/g to about 2,500 m2/g.
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7. The catalyst system of claim 1, wherein the catalyst support comprising the organosilica material has an X-Ray diffraction spectrum exhibiting substantially no peaks above 4 degrees 2θ
- ; and
/or is made using substantially no added structure directing agent or porogen.
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8. The catalyst system of claim 1, wherein the olefin polymerization catalyst compound comprises one or more metallocene compounds represented by the formula:
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TyCpmM6GnX5qwherein each Cp is, independently, a cyclopentadienyl group which may be substituted or unsubstituted, M6 is a Group 4 transition metal, G is a heteroatom group represented by the Formula JR*z where J is N, P, O or S, and R* is a linear, branched or cyclic hydrocarbyl group having from one to twenty carbon atoms and z is 1 or 2, T is a bridging group, and y is 0 or 1, X5 is a leaving group, and m=1 or 2, n=0, 1, 2 or 3, q=0, 1, 2 or 3, and the sum of m+n+q is equal to the oxidation state of the transition metal.
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9. The catalyst system of claim 8, wherein each Cp is a cyclopentadienyl, indenyl or fluorenyl group, which may be substituted or unsubstituted, each M6 is titanium, zirconium, or hafnium, and each X5 is, independently, a halide, a hydride, an alkyl group, an alkenyl group or an arylalkyl group.
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10. The catalyst system of claim 8, wherein y is 1, m is 1, n is 1, J is N, and R* is methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, cyclooctyl, cyclododecyl, decyl, undecyl, dodecyl, adamantyl or an isomer thereof.
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11. The catalyst system of claim 8, wherein the at least one metallocene compound comprises one or more of:
- bis(tetrahydroindenyl)Hf Me2;
bis(1-butyl,3-methylcyclopentadienyl)ZrCl2;
bis-(n-butylcyclopentadienyl)ZrCl2;
(Dimethylsilyl)2O bis(indenyl)ZrCl2;
dimethylsilyl(3-(3-methylbutyl)cyclopentadienyl)(2,3,4,5-tetramethylcyclopentadienyl)ZrCl2;
dimethylsilylbis(tetrahydroindenyl)ZrCl2;
dimethylsilyl-(3-phenyl-indenyl)(tetramethylcyclopentadienyl)ZrCl2;
dimethylsilyl(3-neopentylcyclopentadienyl)(tetramethylcyclopentadienyl)HfCl2;
tetramethyldisilylene bis(4-(3,5-di-tert-butylphenyl)-indenyl)ZrCl2;
cyclopentadienyl(1,3-diphenylcyclopentadienyl)ZrCl2;
bis(cyclopentadienyl)zirconium dichloride;
bis(pentamethyl cyclopentadienyl)zirconiurn dichloride;
bis(pentamethylcyclopentadienyl)zirconium dimethyl;
bis(pentamethylcyclopentadienyl)hafnium dichloride;
bis(pentanmethylcyclopentadienyl)zirconium dimethyl;
bis(1-methyl-3-n-butylcyclopentadienyl)zirconium dichloride;
bis(1-methyl-3-n-butylcyclopentadienyl)zirconium dimethyl;
bis(1-methyl-3-n-butylcyclopentadienyl)hafnium dichloride;
bis(1-methyl-3-n-butylcyclopentadienyl)hafnium dimethyl;
bis(indenyl)zirconium dichloride;
bis(indenyl)zirconium dimethyl;
bis(tetrahydro-1-indenyl)zirconium dichloride;
bis(tetrahydro-1-indenyl)zirconium dimethyl;
dimethylsilylbis(tetrahydroindenyl)zirconium dichloride;
dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl;
dimethylsilylbis(indenyl)zirconium dichloride;
dimethylsilyl(bisindenyl)zirconium dimethyl;
dimethylsilylbis(cyclopentadienyl)zirconium dichloride; and
dimethylsilylbis(cyclopentadienyl)zirconium dimethyl.
- bis(tetrahydroindenyl)Hf Me2;
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12. The catalyst system of claim 1, wherein the activator comprises an alkylalumoxane and/or a non-coordinating anion.
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13. The catalyst system of claim 1, wherein the one or more olefin polymerization catalyst compounds comprises a Ziegler-Natta catalyst compound.
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14. The catalyst system of claim 1, wherein the one or more olefin polymerization catalyst compounds comprises one or more metallocene compounds of:
- dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl;
dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dichloride;
dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)titanium dimethyl;
dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)titanium dichloride;
μ
-(CH3)2Si(cyclopentadienyl)(1-adamantylamido)M7(R15)2;
μ
-(CH3)2Si(3-tertbutylcyclopentadienyl)(1-adamantylamido)M7(R15)2;
μ
-(CH3)2Si(tetramethylcyclopentadienyl)(1-adamantylamido)M7(R15)2;
μ
-(CH3)2C(tetramethylcyclopentadienyl)(1-adamantylamido)M7(R15)2;
μ
-(CH3)2Si(tetramethylcyclopentadienyl)(1-tertbutylamido)M7(R15)2;
μ
-(CH3)2Si(fluorenyl)(1-tertbutylamido)M7(R15)2;
μ
-(CH3)2Si(tetramethylcyclopentadienyl)(1-cyclododecylamido)M7(R15)2;
or μ
-(C6H5)2C(tetramethylcyclopentadienyl)(1-cyclododecylamido)M7(R15)2;where M7 is selected from a group consisting of Ti, Zr, and Hf and R15 is selected from halogen or C1-C5 alkyl.
- dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl;
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15. The catalyst system of claim 1, wherein the one or more olefin polymerization catalyst compounds comprises a first metallocene compound and a second metallocene compound independently selected from the group consisting of:
- SiMe2(Me4Cp)(cC12N)TiMe2 and bis(1-Bu,3-Me-Cp) ZrCl2;
SiMe2(Me4Cp)(cC12N)TiMe2 and (SiMe2) bis(indenyl)ZrCl2;
SiMe2(Me4Cp)(cC12N)TiMe2 and (SiMe2)2O bis(indenyl)ZrCl2;
SiMe2(Me4Cp)(cC12N)TiMe2 and (SiMe2)2O bis(indenyl)ZrMe2;
SiMe2(Me4Cp)(cC12N)TiMe2 and SiMe2(3-neopentylCp)((Me4Cp)HfCl2;
SiMe2(Me4Cp)(cC12N)TiMe2 and SiMe2(3-neopentylcyclopentadienyl)(Me4Cp)HfMe2;
SiMe2(Me4Cp)(1-adamantylamido)TiMe2 and bis(1-Bu,3-MeCp)ZrCl2; and
SiMe2(Me4Cp)(1-t-butylamido)TiMe2 and bis(1-Bu,3-MeCp)ZrCl2.
- SiMe2(Me4Cp)(cC12N)TiMe2 and bis(1-Bu,3-Me-Cp) ZrCl2;
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16. The catalyst system of claim 12, wherein the activator comprises methylalumoxane, ethylalumoxane, N,N-dimethylanilinium tetrakis(pentafluorophenyl) borate, triphenylcarbenium tetrakis(pentafluorophenyl)borate, N,N-dimethylanilinium tetrakis(perfluoronaphthyl)borate, triphenylcarbenium tetrakis(perfluoronaphthyl)borate or a mixture thereof.
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17. A process to produce polymer comprising:
contacting, in the gas phase or slurry phase, one or more olefin monomers with the catalyst system of claim 1; and
ii) obtaining a polymer.
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18. The process of claim 17, wherein the polymer is an ethylene polymer or a propylene polymer.
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19. The process of claim 17, wherein the process occurs at a temperature of from about 0°
- C. to about 300°
C., at a pressure of from about 0.35 MPa to about 10 MPa, and at a time up to 300 minutes.
- C. to about 300°
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20. The process of claim 17, wherein the one or more olefin monomers comprise ethylene and one or more comonomer selected from propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene or a mixture thereof.
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21. The process of claim 17, wherein the 2) catalyst support comprising an organosilica material comprises a plurality of mesopores having an average pore diameter between about 2 nm and about 50 nm and the polymerization occurs within the mesopores.
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2. The catalyst system of claim 1, wherein olefin polymerization catalyst compound is a coordination polymerization catalyst compound.
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Specification
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Current AssigneeExxonMobil Research & Engineering Company (Exxon Mobil Corporation)
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Original AssigneeExxonMobil Research & Engineering Company (Exxon Mobil Corporation)
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InventorsHoltcamp, Matthew W., Day, Gregory S., Sanders, David F., Calabro, David C., Li, Quanchang, Mertens, Machteld M. W.
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Primary Examiner(s)Lee, Rip A
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Application NumberUS15/526,513Publication NumberTime in Patent Office1,257 DaysField of SearchUS Class CurrentCPC Class CodesB01D 15/00 Separating processes involv...B01D 2253/20 Organic adsorbentsB01D 2253/25 Coated, impregnated or comp...B01D 2256/245 MethaneB01D 2257/302 Sulfur oxidesB01D 2257/304 Hydrogen sulfideB01D 2257/40 Nitrogen compoundsB01D 2257/504 Carbon dioxideB01D 2257/80 WaterB01D 53/02 by adsorption, e.g. prepara...B01D 53/0462 Temperature swing adsorptionB01D 53/047 Pressure swing adsorptionB01D 67/0088 Physical treatment with com...B01D 71/702 Polysilsesquioxanes or comb...B01J 20/0229 Compounds of FeB01J 20/0237 Compounds of CuB01J 20/06 comprising oxides or hydrox...B01J 20/08 comprising aluminium oxide ...B01J 20/10 comprising silica or silicateB01J 20/103 comprising silicaB01J 20/16 : Alumino-silicates B01J20/12...B01J 20/18 : Synthetic zeolitic molecula...B01J 20/22 : comprising organic materialB01J 20/262 : obtained otherwise than by ...B01J 20/264 : derived from different type...B01J 20/28011 : Other properties, e.g. dens...B01J 20/28057 : Surface area, e.g. B.E.T sp...B01J 20/28061 : being in the range 100-500 ...B01J 20/28064 : being in the range 500-1000...B01J 20/28066 : being more than 1000 m2/gB01J 20/28069 : Pore volume, e.g. total por...B01J 20/28071 : being less than 0.5 ml/gB01J 20/28073 : being in the range 0.5-1.0 ...B01J 20/28076 : being more than 1.0 ml/gB01J 20/28078 : Pore diameterB01J 20/28083 : being in the range 2-50 nm,...B01J 20/286 : Phases chemically bonded to...B01J 20/3042 : Use of binding agents; addi...B01J 20/3204 : Inorganic carriers, support...B01J 20/3212 : consisting of a polymer obt...B01J 20/3236 : containing metal, other tha...B01J 20/3238 : containing any type of zeoliteB01J 20/3272 : Polymers obtained by reacti...B01J 2220/86 : Sorbents applied to inner s...B01J 23/44 : PalladiumB01J 31/0274 : containing silicon ligands ...B01J 35/615 : 100-500 m2/gB01J 35/617 : 500-1000 m2/gB01J 35/618 : more than 1000 m2/gB01J 35/647 : 2-50 nmB01J 37/0213 : Preparation of the impregna...B01J 37/0236 : Drying, e.g. preparing a su...C01B 37/00 : Compounds having molecular ...C07D 251/30 : Only oxygen atomsC07F 7/0807 : comprising Si as a ring atomC07F 7/081 : comprising at least one ato...C08F 210/02 : EtheneC08F 210/14 : Monomers containing five or...C08F 210/16 : Copolymers of ethene with a...C08F 4/02 : Carriers thereforC08F 4/027 : PolymersC08F 4/64013 : NNC08F 4/64048 : NOC08F 4/64089 : NNNC08F 4/64148 : NN(R)NC08F 4/64158 : ONOC08F 4/64189 : ONNOC08F 4/64193 : OOOOC08F 4/659 : Component covered by group ...C08F 4/65912 : in combination with an orga...C08F 4/65916 : supported on a carrier, e.g...C08F 4/6592 : containing at least one cyc...C08F 4/65925 : two cyclopentadienyl rings ...C08F 4/65927 : two cyclopentadienyl rings ...C08G 77/26 : nitrogen-containing groupsC08G 77/60 : in which all the silicon at...C10G 25/003 : Specific sorbent material, ...C10G 31/09 : by filtrationC10G 35/06 : characterised by the cataly...C10G 45/00 : Refining of hydrocarbon oil...C10G 45/04 : characterised by the cataly...C10G 45/34 : characterised by the cataly...C10G 45/44 : Hydrogenation of the aromat...C10G 45/46 : characterised by the cataly...C10G 45/52 : containing platinum group m...C10G 45/60 : characterised by the cataly...C10G 45/64 : containing crystalline alum...C10G 47/02 : characterised by the cataly...C10G 50/00 : Production of liquid hydroc...C10K 1/32 : with selectively adsorptive...C10M 101/02 : Petroleum fractionsC23C 16/56 : After-treatmentY02C 20/40 : of CO2