CA1327347C

CA1327347C - Method for preparing a supported metallocene-alumoxane catalyst for gas phase polymerization

Info

Publication number: CA1327347C
Application number: CA000584347A
Authority: CA
Inventors: Main Chang
Original assignee: Exxon Chemical Patents Inc
Current assignee: ExxonMobil Chemical Patents Inc
Priority date: 1987-12-17
Filing date: 1988-11-28
Publication date: 1994-03-01
Anticipated expiration: 2011-03-01
Also published as: DE3874310T2; EP0323716A1; DE3874310D1; KR890009985A; IL88494A; IL88494A0; HUT48912A; YU228288A; NO885363L; NO885363D0; JPH01207303A; PL276458A1; PT89232B; BR8806673A; AU2596188A; AU621320B2; FI885570A; JP2816469B2; DK677488A; ATE80167T1

Abstract

ABSTRACT OF THE DISCLOSURE
This invention relates to a process for preparing a supported metallocene alumoxane catalyst for use in the gas phase polymerization of olefins. The invention particularly relates to the use of silica gel containing from about 6 to about 10 percent by weight adsorbed water as the catalyst support material. It has been found that such silica gel may be safely added to an aluminum trialkyl solution to form by direct reaction with the adsorbed water content of the silica gel catalyst support material the alumoxane component of the catalyst system. An alumoxane coated silica gel is formed to which a metallocene may be added and the resulting material dried to free flowing powder. The dry free flowing powder may then be used as a supported metallocene alumoxane catalyst complex for gas phase polymerization of olefins.

Description

~32734~

, .
1 This invention relates to a process for preparing a 2 supported metallocene alumoxane catalyst for use in the gas phase 3 polymerization of olefins. The invention particularly relates to the use of silica gel containing from about 6 to about lO percent by weight adsorbed water as the catalyst support material. It has , 6 been found that such silica gel may be safely added to an aluminum ~ 7 trlalkyl solution to form, by direct reaction with the adsorbed - 8 water content of the silica gel catalyst support material, the ,..................................... .
g alumoxane component of the catalyst system. An alumoxane coated silica gel is formed to which a metallocene may be added and the 11 resulting material dried to free flowing powder. The dry free ~$~ 12 flowing powder may then be used as a supported metallocene 13 alumoxane catalyst complex for gas phase polymerization of olefins.
-~ 14 Backaround to the Invention ' 15 Olefin polymerization catalysts comprising a metallocene ~ 16 and an aluminum alkyl component were first proposed in about 1956.', 17 Australian patent 2436/88 proposed for use as a polymerization 18 catalyst a bis-(cyclopentadienyl) titanium, zlrconium, or vanadium 9 salt as reacted with a variety of halogenated or unhalogenated ;~ 20 aluminum alkyl compounds. Although such complexes were capable of 21 catalyzing the polymerization of ethylene, such catalytic 22 complexes, especially those made by reaction with an aluminum ~ 23 trialkyl, had an insufficient,level of catalytic actiYity to be '?'.~ 24 employed commercially for production of polyethylene or copolymers '. 25 of ethylene.
$ 26 Later it was found that certain metallocenes such as ;i 27 bis-(cyclopentadienyl) titanium, or zirconium dialkyls in ~; 28 combination ~ith aluminum alkyl/water cocatalyst form catalyst ;~ 29 systems for the polymerization of ethylene. Such catalysts are discussed in German Patent DE 2,608,863 published 9 September 1977 t 31 which disc:loses a : ,.
.:
5,~
?.
;1 ~
:~ ~

' ' 13273~7 1 polymerization catalyst for ethylene consisting of 2 bis-(cyclopentadienyl) titanium dialkyl, aluminum trialkyl and 3 water. German Patent DE2,608,933 published 9 Sept.1977 discloses an ethylene 4 polymerization catalyst consisting of a cyclopentadienyl zirconium salt, an aluminum trialkyl cocatalyst and water. European Patent 6 Application No. 0035242 published 9 Sept.1991 discloses a process fo~ preparing 7 ethylene and atactic propylene polymers in the presence of a halogen free 8 cyclopentadienyl transition metal salt and an alumoxane. Such 9 catalysts have sufficient activity to be commercially useful and enable the control of polyolefin,molecular weight by means other 11 than hydrogen addition--such as by controlling the reaction 12 temperature or by controlling the amount of cocatalyst alumoxane as 13 such or as produced by the reaction of water with an aluminum alkyl.

14 To realize the benefits of such catalyst systems, one must use or produce the required alumoxane cocatalyst component. An 16 alumoxane is produced by the reaction of an aluminum alkyl ~ith 17 water. The reaction of an aluminum alkyl with water is very rapid 18 and highly exothermic. Because of the extreme violence of the 19 reaction the alumoxane cocatalyst component has, heretofore, been separately prepared by one of two general methods. Alumoxanes may 21 be prepared by adding an extremely finely divided water, such as in 22 the form of a humid solvent, to a solution of aluminum alkyl in 23 benzene or other aliphatic hydrocarbons. The production of an 24 alumoxane by such procedures requires use of explosion-proof equipment and very close control of the reaction conditions in 26 order to reduce potential fire and explosion hazards. For this 27 reason, it has been preferred to produce alumoxane by reacting an 28 aluminum alkyl with a hydrated salt, such as hydrated copper 29 sulfate In such procedure a slurry of finely divided copper sulfate pentahydrate and toluene is formed and mantled under an 31 inert gas. Aluminum alkyl is then slowly added to the slurry with 32 stirring and the reaction mixture ls mainta1ned at room temperature 33 for 24 to 48 hours during which a slow hydrolysls occurs by which 34 alumoxane is produced. Although the production of alumoxane by a hydrated salt method slgnificantly reduces the explosion and fire 36 hazard inherent in the wet solvent production method, production of 37 an alumoxane by reaction with a hydrated salt must be carried out : `

1327~7 1 as a process separate from that of producing the metallocene 2 alumoxane catalyst ~tself, is slow, and produces hazardous wastes 3 that create disposal problems. Further, before the alu~oxane can 4 be used for the product~on of an active catalyst complex the hydrated salt reagent must be separated from the alumoxane to 6 prevent lt from becomlng entrained in the catalyst complex and thus 7 contaminat~ng any polymer produced therewith.
8 Only in those situat~ons where~n a hydrated material ~s of 9 a chemical compos~tlon acceptable as a filler mater~al for a filled polyolefln composlt~on may it be used to produse a 11 metallocene/alumoxane catalyst complex by direct reaction with an 12 aluminum alkyl solut~on. Hence U.S. Patent 4,431,788 d~scloses a 13 process for produc~ng a starch filled polyolefin composition 14 where~n an aluminum trialkyl 1s first reacted wlth starch particles of a moisture content below 7 we~ght percent. The starch particles 16 are then treated with a (cyclopentadienyl)-chromium, titanium, 17 vanad~um or zircon~um alkyl to form a metallocene alumoxane 18 catalyst complex on the surface of the starch partlcles. An olef~n 19 ~s then polymerized about the starch particles by solution or suspension polymerizat~on procedures to form a free-flow1ng 21 composition of polyolef1n-coated starch part~cles. German Patent 22 3,240,382 likew~se d~scloses a method for produc~ng a f111ed 23 polyolefln composit~on wh~ch ut~l~zes the water content of an 24 1norgan~c flller mater1al to d~rettly react with an alum~num trlalkyl and produce thereon an active metallocene alumoxane 26 catalyst complex. Polymer ~s produced by solution or gas phase 27 procedures at the f~ller surface to un~formly coat the flller 28 particles and provlde a f~lled polymer composlt10n.
29 ~erman Patent 3,240,382 notes that the activ~ty o~ a metallocene alumoxane catalyst ~s greatly tmpalred or lost when 31 prepared as a surface coat~ng on an ~norgan~c material. Although 3~ ~erman Patent 3,240,382 suggests that an ~norganic mater1al 33 conta~n1ng absorbed or adsorbed water may be used as a f~ller 34 materlal from which the alumoxane cocatalyst component may be prepared by d~rect r~act~on w~th an alum~num tr~alkyl, the only 36 water contaln~ng lnorgan~c f~ller mater~als ~hlch are ~dent~f~ed as 37 capable of produclng the alumoxane ~thout adversely affectlng the ,.~

~ 3273~7 1 activity of the metallocene alumoxane catalyst complex are certain 2 inorganic materials containing water of crystallization or bound 3 water, such as gypsum or mica. German Patent 3,240,382 does not 4 illustrate the production of a catalyst coated inorganic filler material wherein the inorganic ~aterial is one having absorbed or ~ adsorbed water. Nor does German Patent 3,240,382 describe an 7 inorganic filler material having absorbed or adsorbed water which 8 has surface area or pore vo1ume properties suitable for service as 9 a catalyst sùpport for a gas phase polymerization procedure.
It would be desirable to devise an economical procedure 11 whereby an active supported metallocenelalumoxane catalyst could be 12 safely produced for use as a gas phase polymerization catalyst. To 13 be economical the procedure should dispense with the requirement of 14 producing the alumoxane component as a separate component apart from the procedure by which the catalyst itself is prepared.
16 Summary of_the Invention 17 The process of this invention utilizes as the catalyst 18 support material silica particles preferably having a sur~ace 19 area in the range of about 10 m2/g to about 700 m2/g, more preferably about 100-500 m2/g and desirably about 200-400 21 m2~g, a pore volume preferably of about 3 to about 0.5 cc/g 22 and more preferably 201 cc/g and an adsorbed water content 23 preferably of ~rom about 6 to about 10 weight percent, ~ore 24 preferably from about 7 to about 9 weight percent, and most preferably about 8 weight percent. Such sil~ca particles are 26 referred to hereafter as an undehydrated sillca gel. The silica 27 gel supported metallocene alumoxane catalyst is prepared by adding z8 the undehydrated s~lica gel to a stirred solution of aluminum 29 trialkyl in an amount sufficient to provide a mole ratio of aluminum trial':yl to water of from about 3:1 to about 1:2, 31 preferably 1.2:1 to about 0.9:1; thereafter adding to this stirred 32 solution a metallocene in an amount sufficient to provide an 33 aluminum to transitional metal ratio of ~referably from about lO00:1 to 1:1, 34 more preferably from ab~ut 300:1 to 10:1, most preferably fro~-about 150:1 to about 30:1; removlng the solvent and drying the solids to 36 a free flowing po~der. Drying can be obta~ned by modest heating or 37 vacuum.

. .

132734 ~

l The dr~ed free flow~ng powder compr~ses a metallocene 2 alumoxane catalyst complex adsorbed upon the surface of the slllca 3 gel support particles. The supported catalyst complex has an 4 act~vity sufficient for use as a gas phase polymerizat~on catalyst for polymerization of olefins by convent~onal gas phase 6 polymerization procedures.
7 Detailed Descr~1ption of the Preferred Embodim~nts 8 The present invent~on ~s d~rected towards a method for 9 prepar~ng a supported catalyst system for use 1n the gas phase polymerization of oleflns, part~cularly the gas phase 11 polymerlzation of ethylene to h1gh molecular weight polyethylenes 12 such as linear low density polyethylene (LLDPE) and h~gh denslty 13 polyethylene (HDPE). The polymers are ~ntended for fabr1cat~on 14 1nto art~cles by extrus~on, in~ection molding, thermoforming, lS rotatlonal molding, and the 11ke. In particular, the polymers 16 prepared with the catalyst complex and by the method of th~s 17 ~nvention are homopolymers of ethylene and copolymers of ethylene 18 with hlgher alpha-olefins havlng from 3 to about lO carbon atoms 19 and preferably 4 to 8 carbon atoms. Illustrat~ve of the h~gher alpha-olefins are butene-l, hexene-l, and octene-l.
21 In the process o~ the present invention, ethylene, e~ther 22 alone or together w~th alpha-olef~ns having three or more carbon 23 atoms, is polymer1zed in the presence of a s~llca gel supported 24 catalyst system compr~s~ng at least one metallocene and an alumoxane.
26 In accordance w~th this invent1On, one can also produce 27 olef~n copolymers, part~cularly copolymers of ethylene and h~gher 28 alpha-olefins having from 3-18 carbon atoms.
29 The act~ve catalyst complex ~ epared by the proce~s of thls 1nvention compr1ses a metallocene and an alumoxane adsorbed 31 onto the surface of a s111ca gel support mater1al. Alumoxanes are 3~ ollgomerk alum1num compounds represented by the general formula 33 (R-Al-O)y whlch ~s belleved to be a cycl1c compound and 34 R(R-Al-0-)yAlR2, wh1ch ~s a l~near compound. In the general 3S formula, "R" ~i a Cl-ClO alkyl group such as, for example, 36 ~ethyl, ethyl, propyl, butyl, and pentyl and Uy" ~s an ~nteger from 37 2 to about 30 and represents the degree of ol~gomer1zatlon of the ;

; 13273~7 , l alumoxane. Preferably, "R" 1s methyl and "y" 1s about 4 to about 2 25 and most preferably 6-25. Generally, in the preparat10n of 3 alumoxanes from, for example, the reaction of alumlnum trimethyl 4 and water, a mixture of linear and cycl1c compounds ls obta1ned.
Generally, an alumoxane having a hlgher degree of ol190mer~zation 6 w111, for a given metallocene, produce a catalyst complex of higher 7 act1v1ty than will an alumoxane having a lower degree of 8 ol1gomerk at~on. Hence, the procedure by wh1ch alumoxane 1s g produced by direct reaction of an alum1num tr1alkyl ~lth an undehydrated s111ca gel should 1nsure the convers10n of the bulk 11 quantity of the aluminum trlalkyl to an alumoxane havlng a high 12 degree of ol190mer1zat10n. In accordance with th1s 1nYent~on the 13 des1red degree of oligomer1zat10n 1s obtained by the order of 14 addition of reactants as descr1bed here1nafter.
~, 15 The metallocene may be any of the organometall1c 16 coordination compounds obta1ned as a cyclopentad1enyl derivative of 17 a transition metal. Metallocenes which are useful for prepar1ng an 18 act1ve catalyt1c complex accord1ng to the process of th1s 1nvention 19 are the mono, bl and tr1 cyclopentad1enyl or substituted cyclopentadienyl metal compounds and most preferably, 21 bi-cyclopentadienyl compounds. The metallocenes part1cularly 22 useful in this 1nvent10n are represented by the general formulas:

24 I. (Cp)mMRnXq $
wherein Cp is a cyclopentad1enyl r1ng, M 1s a Group 4b or 5b 26 trans1tion metal and preferably a ~roup 4b trans1t10n metal, R 1s a 27 hydrocarbyl group or hydrocarboxy group hav1ng from l to 20 carbon 28 atoms, X 1s a halogen, and ,n 1s a whole number from l to 3, n 1s a 29 whole number from 0 to 3, and q 1s a whole number from 0 to 3, II. (C5Rlk)gR s(C5R k)MQ3_g `~ 31 III- R"s(C5R'k)2MQ' 3~ where1n ~C5R'k) ls a cyclopentad1enyl or subst1tuted 33 cyclopentad1enyl, each R' 1s the ~ame or dlfferent and 1s hydrogen `''':
.

.~

., 1 or a hydrocarbyl radical such as alkyl, alkenyl, aryl, alkylaryl, 2 or ary1alkyl radicals containing from 1 to 20 carbon atoms, a 3 silicon-conta~ning hydrocarbyl radical, or a hydrocarbyl radical 4 wherein two carbon atoms are joined together to form a C4-C6 ring, R" is Cl-C4 alkylene radical, a dialkyl germanium ~r 6 silicone, or an alkyl phosphine or amine radical bridsin3 two 7 (C5R'k) rings, Q is a hydrocarbyl radical such as aryl, alkyl, 8 alkenyl, alkylaryl, or arylalkyl having 1-20 carbon atoms, g hydrocarboxy radical having 1-20 carbon atoms or halogen and can be the same or different, Q' is an alkylidene radical having from 1 to 11 about 20 carbon atoms9 s is 0 or 1, g is 0, 1 or ?; when g is 0, s 12 ~s 0; k is 4 when s is 1 and k is 5 when s is 0 and M is as defined 13 above.
14 Exemplary hydrocarbyl radicals are methyl, ethyl, propyl, butyl, amyl, isoamyl, hexyl, isobutyl, heptyl, octyl, nonyl, decyl, 16 cetyl, ~-ethylhexyl, phenyl, and the like. Exemplary alkylene 17 radicals are methylene, ethylene, propylene, and the like.
18 Exemplary halogen atoms ~nclude ch10r1ne, bromine and iodine and of 19 these halogen atoms, chlorine ls preferred. E~emplary of the alkylidene radicals is methylidene, ethylidene and propylidene.
21 Of the metallocenes, zirconocenes and titanocenes are most 22 preferred. Illustrative but non-11mlting examples of these 23 metallocenes which can be use~ully employed ~n accordance with th~s 24 ~nvention are monocyclopentadienyl titanocenes such as, cyclopentadienyl titan~um trichloride, pentamethytcyclopentadienyl 26 titanium trich10r~de; bis~cyclopentad1enyl) titanium dlphenyl; the 27 carbene represented by the formula Cp2Ti.CH2 Al(CH3)2Cl 28 and derivatives of thls reagent such as Cp2Ti.CHz Al(CH3)3, P2 iCH2)2~ CP2TiCH2CH(CH3)CH2. Cp2T~cHcH2cH2~
Cp2Tl~CH~ AlR" '2Cl, wherein Cp is a cyclopentadienyl or 31 substltuted cyclopentadienyl rad~cal, and R" ' is an alkyl, aryl, 32 or alkylaryl rad~cal hav~ng from 1-18 carbon atoms; substituted 33 b~s(Cp)T~(IV) compounds such as b1s(indenyl)T~ diphenyl or 34 dlchlor~de, bis(methylcyclopentadienyl)T~ diphenyl or dlhalides and other dihal~de complexes; d1alkyl, trialkyl, tetra-alkyl and 36 penta-alkyl cyclopentad1enyl t~tanium compounds such as 37 b~s(l,2-d~methylcyclopentadlenyl)r1 dlphenyl or dichlor1de, ~`

13273~7 1 bis(l,2-diethylcyclopentadienyl)T~ diphenyl or dichloride and other 2 dihalide complexes; sil~cone, phosph~ne, amine or carbon bridged 3 cyclopentadiene complexes, such as dimethyl s~lyldicyclopentadienyl 4 titanium diphenyl or dichloride, methylenedicyclopentadienyl titanium diphenyl or dichloride and other dihal~de complexes and 6 the like.
7 Illustrative but non-limitin~ examples of the zirconocenes 8 which can be usefully employed ln accordance wlth thls ~nvention 9 are cyclopentadlenyl z~rcon~um trichloride, pentamethylcyclo-pentadienyl zirconium trichloride, b~s(cyclopentadienyl)zircc,nium 11 diphenyl, bls(cyclopentadienyl)z~rcon~um dichloride, the alkyl 12 substituted cyclopentadienes, such as bis(ethyl 13 cyclopentadieny1)zirconium d~methyl, bis(B-phenylpropylcyclo-14 pentad~enyl)zlrconium d~methyl, bls(methylcyclopentadlenyl) z~rconium d~methyl, and dihal~de complexes of the above; d1-alkyl, 16 tr~-alkyl, ~etra-alkyl, and penta-alkyl cyclopentadienes, such as 17 bis(pentamethylcyclopentad~enyl)zirconium dimethyl, b~s(l,2-di-18 methylcyclopentadienyl)zlrconlum d~methyl, bis(l,3-d7ethylcyclo-19 pentadienyl)zirconium dimethyl and dihalide complexes of the above;
silicone, phosphorus, and carbon br~dged cyclopentad~ene complexes 21 such as dlmethylsllyldicyclopentadienyl z~rconium dimethyl or 22 dlhalide, methylphosph~ne d~cyclopentadlenyl z~rconium d~methyl or 23 d1halide, and methylene d~cyclopentad~enyl z~rconium d~methyl or 24 dihal~de, carbenes represented by the formulae Cp2Zr.CH2P(C6H5)2CH3, and der~vat~ves of these compounds such as Cp~t~CH2CH(CH3)~H2.
26 B~s(cyclopentad~enyl)hafn~um d1chlor~de, b~s(cyclopenta-27 dlenyl)hafnium dimethyl, bls(cyclopentad~enyl)vanadium dlchlor1de 28 and the l~ke are ~llustrat1ve of other metallocenes.
29 Generally the use of a metallocene hh~ch compr~ses a b~s(subst~tuted cyclopentadlenyl) z~rcon1um wlll prov1de a catalyst 31 complex of higher act~v1ty than a correspond~ng t~tanocene or a 32 mono cyclopentad~enyl metal compound. Hence b~s(subst1tuted 33 cyclopentad~enyl) z~rconlum compounds are preferred for use as the 34 metallocene.
, .s,~

-~' ~' ~, ` - 9- 1327347 1 Heretofore the alumoxane component of the active catalyst2 complex has been separately prepared then added as such to a 3 catalyst support mater~al which is then treated with a metallocene 4 to form the active catalyst complex. One procedure heretofore employed for preparing the alumoxane separately ls that of 6 contacting water in the form of a moist solvent with a solution of 7 alum;num trialkyl in a suitable organic solvent such as benzene or 8 aliphatic hydrocarbon. As before noted this procedure is attendant g w;th fire and explosion hazards which require the use of explosion-proof equipment and carefully controlled reaction 11 conditions~ In an alternative method heretofore employed for the 12 separate production of alumoxane, an aluminum alkyl ~s contacted 13 with a hydrated salt, such as hydrated copper sulfate. The method 14 compr~sed treating a dilute solut~on of aluminum alkyl in, for example, toluene with a copper sulfate pentahydrate. A slow, 16 controlled hydrolys~s of the aluminum alkyl to alumoxane results 17 wh~ch substantially ellm~nates the f~re and explosion hazard but 18 with the disadvantage of the creation of hazardous waste products 19 that must be disposed of and from wh~ch the alumoxane must be separated before lt is sultable for use ~n the production of an 21 active catalyst complex. Separate production of the alu~oxane 22 component by either procedure ~s time consum~ng and costly.
23 Correspondingly, the use of a separately produced alumoxane greatly 24 ~ncreases the cost of produclng a metallocene alumoxane catalyst.
In accordance ~th the present invention the alumoxane 2~ component of the catalyst complex 1s prepared by direct react~on of 27 an alum~num tr~alkyl with the material ut~l~zed as the catalyst 28 support, namely an undehydrated s~l~ca gel. S11~ca useful as the 29 catalyst support is that which preferably has a surface area in the range of about 10 to about 700 m2/g, more preferably 31 about 100-500 and desirably about 200-400 m2/g, a pore volume 32 ~referably of about 3 to about 0.5 cc/g and more preferably 33 2-1 cc/g, and an adsorbed water content pre~erably of from 34- about 6 to about 10 weight percent, more preferably from about 7 to about 9 weight percent, and most preferably about 36 7.5 to about 8.5 weight percent. The particle size of the 37 silica should be from about 10~ to about lOOu, and preferably 38 from about 30~ to about 60~ = 10 6m). Hereafter, silica 39 having the above identified properties is referred to as undehydrated silica gel.

1 Undehydrated silica gel, as def~ned above, ~s added over 2 t~me, about a few m~nutes, to a stirred solut~on of alumlnum 3 trlalkyl, preferably trimethyl alumlnum or triethyl aluminum, in an 4 amount sufficient to provlde a mole ratlo of alum~num tr~alkyl to water of from about 3:1 to 1:2, preferably about 1.2:1 to 0.9:1.
6 The solvents used in the preparation of the catalyst system are 7 inert hydrocarbons, in particular a hydrocarbon that ~s lnert with 8 respect to the catalyst system. Such solvents are well known and 9 ~nclude, for example, isobutane, butane, pentane, hexane, heptane, octane, cyclohexane, methylcyclohexane, toluene, xylene and the 11 l~ke. Also su~table for use as the alum1num tr~alkyl are tripropyl 12 alum~num, tri-n-butyl aluminum tr~-~sobutyl alum~num, 13 trl(2-methyl-pentyl) alum~num, trlhexyl alum~num, tr~-n-octyl 14 aluminum, and tri-n-decyl alum1num.
Upon addit~on of the undehydrated s71ica gel to the 16 solution of aluminum trialkyl, the water content of the sil~ca gel 17 controllably reacts with the aluminum tr~alkyl to produce an 18 alumoxane whieh ~s deposlted onto the surface of the silica gel 19 particles. Although the react~on of the aluminum tr~alkyl with the water content of the s11ica gel proceeds relatively qu~ckly, that 21 ~s, ~t ~s generally completed w~thin the t~me of about S minutes, 22 lt does not occur with the explos~ve qu1ckness of that wh1ch occurs 23 wlth free water. The react~on may be safely conducted ln 24 conventlonal mix1ng equ1pment under a mantle of ~nert gas.
Thereafter a metallocene ~s added to the st~rred 26 suspens~on of alumoxane sll~ca gel product ~n an amount suff~cient 27 to prov~de a mole ratlo of alum~num to trans~t~on metal of from 28 about 1000:1 to about 1:1, preferably from about 300:1 to about 29 10:1 and most preferably .rom about 150:1 to about 30:1. The mixture ls st~rred for about 30 m~nutes to about one hour at 31 amb~ent or an elevated temperature of about 75C to permlt the 32 metallocene to undergo complete complexlng react~on w1th the 33 adsorbed alu~oxane. Thereafter, the solvent ~s removed and the 4 residual sol1ds are drled, preferably at a temperature of 75-C or greater, to a free flowlng powder. The free flow~ng po~der 36 compr~es a s~l ka gel supported metallocene ~lumoxane catalyst 37 complex of suff~c~ently h~gh catalyt~c activ~ty for use ~n the gas ,~
.~

.~
;

13273~7 1 phase polymerizatlon of olef~ns by conventional gas phase 2 polymerization procedures.
3 The order of additlon between the undehydrated silica gel 4 and the aluminum tr~alkyl ~s important with regard to the act~v~ty of the supported catalyst whlch results upon add~tion of the 6 metallocene. A supported catalyst compositlon of little or no 7 activity results where~n an alum~num tr~alkyl is added to a st~rred 8 solvent suspenslon of undehydrated s11~ca gel. It has been found 9 that to prepare a supported catalyst compos~t~on of acceptable or h~gh act~v~ty the order of mlx~ng must be one wherein the 11 undehydrated s~l~ca gel ~s added to a stirred solution of the - 12 alum~num tr~alkyl. It is bel~eved that thls order of mix~ng forces 13 the aluminum trialkyl to undergo reactlon in the context of a 14 transient localized excess of alum~num trialky1 compared to a ~;~ 15 transient localized deflc~ency of water. Under a mixing condition16 wh~ch slowly adds undehydrated s~llca get to a stirred solut~on of 17 aluminum trialkyl, the bulk content of the alum~num trialkyl j 18 converts to an alumoxane wlth a degree of ol~gomerization of abouti~ 19 6-25 (y ~ 6-25). Production of an alumoxane with this degree of oligomerizatlon results ~n a flnal metallocene alumoxane catalyst ~i- 21 complex of useful or h~gh act~vity. A reverse order of mlx1ng, x 22 that is, add~tion of an alum1num trialkyl to a st~rred solvent 23 suspens~on ~f undehydrated s~llca gel yields a catalyst wh1ch has a ~ 24 poor degree of catalytlc activity.
In additlon to the 1mportance of proper mix1ng order in 26 ach~eving a supported catalyst of useful activ~ty, lt has also been 27 observed that the water content of the undehydrated s111ca gel ~ 28 influences flnal catalyst actlv~ty. Hence the undehydrated slllca -/ ~9 gel should have an adsorbed water content of from about 6 to about 10 welght percent. Preferably the adsorbed water content should be 31 from about 7 to about 9 we19ht percent. Maxlmum catalyst actlvlty 32 for a g~ven metallocene component ils generally observed where~n the 33 adsorbed ~ater content of the undehydrated stllca gel used as a 34 support ls from about 7.5 to about 8.5 ~elght percent.
Further lnfluenclng the degres of actlvlty attalned iln the 36 f~nal supported catalyst complex 1s the mole rat~o of alum~num 37 tr1a1kyl to the adsorbed water content of the undehydrated s~llca --` 13273~7 1 gel. The quantities of aluminum tria1kyl employed should, ln 2 comparison to the quantity of undehydrated sillca gel of specified 3 adsorbed water content, be selected to provide a mole ratio of 4 aluminum trialkyl to water of from about 3:1 to about 1:2, preferably from about 1.5:1 to about 0.8:1, more preferably from 6 about 1.2:1 to about 0.9:1, an~ most preferably about 1.1:1 to 7 1.0:1. It has been observed tha$ for a given metallocene, a 8 maximum catalyst act~vity is general1y observed ~n the alumtnum g trialkyl to water mole rat~o range of about 1.2:1 to about 0.9:1.
Depending upon the partlcular aluminum trtalkyl selected for use, 11 commerclally acceptable catalyst actlv~t~es are exh~bited ~n the 12 aluminum trlalkyl to water mole ratlo range of about 3:1 to about 13 1:2.
14 Also lnfluenclng the cost of productlon and the level of catalyt~c activity obta7ned ~n the f~nal supported catalyst complex 16 ls the mole ratlo of aluminum to transitlon metal of the 17 metallocene component. The quantity of metallocene added to the 18 alumoxane adsorbed sl11ca gel solids should be selected to provlde 19 an aluminum t9 transltion metal mole rat1O of from about 1000:1 to ,,~
about 1:1, preferably from about 300:1 to about 10:1, and most 21 preferably from about 150:1 to about 30:1. From the standpotnt of 22 econom1c cons~derations lt ls desirable to operate 1n the lower 23 ranges of the alumlnum to transition metal mole ratlo 1n order to 24 m~nlm~ze the cost of catalyst production. The procedure sf thls lnYention is one whlch prov~des the maxlmum converslon of tne 26 alumlnum trlalkyl component to the most efflcacious form of 27 alumoxane, hence permlts the safe productton of a supported 28 metallocene alumoxane catalyst of useful actlv1ty wlth low 29 quantlt~es of the costly alumlnum tr1alkyl component.
By approprtate selectlon of the type and relative amounts 31 of the metallocene and the alum1num tr1alkyl cocatalyst precursor, 32 one can attaln by the present method the part1cular actlYe catalyst 33 complex deslred for any partlcular applicat~on. For example, 34 hlgher concentrations of alumoxane tn the tatalyst system generally result 1n h1gher ~olecular ~elght polymer product. Therefore, ~hen 36 lt ls deslred to produce a hlgh molecular ~elght polymer a h19her 37 concentratlon of alumlnum trlalkyl ls used, relat1ve to the .

,~

-- 132~3~7 :`

1 metallocene, than when it is des~red to produce a lower molecular 2 weight material. For rost applicat~ons the rat~o of aluminum ~n 3 the aluminum alkyl to total metal ~n the metallocene can be ~n the 4 range of from about 300:1 to about 20:1, and preferably about 200:1 to about 50:1.
6 Follow~ng the addition of the metallocene to the alumoxane adsorbed on the silica gel sol~ds, the solvent is removed by 8 flltering or evaporation, and the res~dual sol~ds are dr~ed to a g free flowing powder. Dry~ng of the residua1 solids may be 1~ conducted at a temperature up to about 85C, and preferably at a 11 temperature of about 75C. The dr~ed free flowing powder comprises 12 a metallocene alumoxane complex adsorbed upon the surface of the 13 s~lica gel support particles. The dr~ed state compositlon exh~bits 14 a level of catalytlc activ~ty useful for ~as phase polymerlzation Of olefins.
16 As known, the molecular weight of the polymer product 17 can be controlled by the ~udlc1Ous selectlon of substltuents on the 18 cyclopentadlenyl rlng and use of l~gands for the metallocene.
19 Further, the comonomer content can be controlled by the ~udic~ous selection of the metallocene. Hence, by the select~on of catalyst 21 components ~t is possible to ta~lor the polymer product with 22 respect to molecular we~ght and density. Further, one may ta~lor 23 the polymerlzat~on react~on cond~tions over a wlde range of 24 condit~ons for the product~on of polymers havlng part~cular propertles.
26 In the examples follow~ng, the melt index (MI) and melt 27 index ratlo (MIR) were determ~ned ~n accordance wlth ASTM test 28 D-1238.
29 Exam~le 1 (Comparatlve) Flve L of methyl alumoxane (4 wt.X ~n toluene), prevlously 31 prepared by react~on of tr~methyl alumlnum ~lth ~ater ln toluene, 3~ ~s added slowly to 1.5 Kg of dehydrated s111ca gel. The sll k a gel 33 was Davison 948 s111ca gel wh~ch had been dehydrated at 800C for 34 20 hours. Followlng add1tlon of the methyl alumoxane, the s~llca gel suspenslon was stlrred for l.Q hours at room temperature.
36 Thereafter, 300 mls of a 13 ~t.X toluene solut10n of b~s(n-butyl-13273~7 1 cyclopentadienyl~ zirconium dichlor~de ~hereinafter 2 (nBuCp)2ZrC12~ was slowly added to the stirred suspension of 3 s~l~ca gel solids and st~rring was con~ nued for 0.5 hours at 4 75C. Thereafter, the volat~le solvent was evaporated by n~trogen purge at 85C to a free flowing powder.
6 The resulting free flowlng powder comprised a metallocene 7 alumoxane catalyst complex supported on sll~ca gel where~n the 8 ratlo of aluminum to zlrconium ~s 50:1. Th~s free flowing powder g was utillzed as a catalyst for the gas phase polymerization of ethylene under the cond~t~ons and w~th the results as set forth ln 11 Table I and the discuss~on thereof.
12 Example 2 13 Undehydrated silica gel was employed ln accordance with 14 the procedure of th~s ~nvent~on to prepare a sil~ca gel supported (nBuCp)2ZrC12 methyl alumoxane cata1yst complex, as follows:
16 Two hundred-sixty (260) mill~l~ters of trimethylalumlnum/
17 heptane solut~on ~15X~ and 3D0 ml of heptane are charged lnto a 18 dr~ed one-l~ter three-neck flask conta~n1ng a magnetic st~rr1ng 19 bar. Thereafter 100 9 of undehydrated sillca gel ~Dav~son 94B) which contains 7.63 wt.~ water ~s added slowly ~nto the flask 21 through a solids additlon vessel. The resulting mixture ~s allowed 22 to react under st~rr~ng at room temperature for 1 hour. Thereafter 23 2.50 9 of (nBuCp)2ZrC12 d~ssolved ~n 120 ml heptane ~s ~n~ected 24 lnto the flask and the resultlng mlxture 1s allowed to react under st~rrlng for 30 mlnutes. The volatlle solvent ~s then removed by 26 nitrogen purging at 75-C and the res1dual sol~ds are drled to a 7 free flow1ng powder by vacuum drylng at amb~ent temperature.
28 The resultlng free ~low~ng powder compr~sed a metallocene 29 methylalumoxane catalyst complex supported on a s11ica gel where~n the mole rat~o of alum~num to z1rconlum 1s 67.4:1. Th~s powder was 31 ut~lized as a catalyst for the gas phase polymer~zation of ethylene 32 under the cond~t~ons and w~th the results set forth 1n Table I and 33 the discussion thereof.
34 Exam~le 3 The procedure of Example 2 ~as follo~ed wlth the except~on 36 that the undehydrated s~llca gel (Dav~son 948) contalned 7.79 ~t.X
37 water.
.,,; .

13273~7 ;

1 Example 4 2 The procedure of Example 2 was followed with the except~on 3 that the undehydnated silica gel (Davison 948) contained 7.16 wt.X
4 water.
Example 5 6 The procedure of Example 2 was followed with the exception 7 that the undehydrated silica gel (Dav~son 948) conta~ned 7.38 wt.X
8 water.
9 Example ~ (Comparative) The procedure of Example was followed with the exception 11 that the trimethylaluminum/heptane solution (15X) ~s charged into a 12 one-l~ter three-neck flask conta~n~ng lO0 9 of undehydrated s~lica 13 gel (Davison 948) wh~ch conta~ns 7.38 wt.~ water and 300 ml of 14 heptane.
Example 7 16 The procedure of Example 2 was followed wlth the except~on 17 that 260 ml of triethylalum1num/heptane solut~on (25X) ls charged 18 into a one-liter flask followed by the addition of lO0 9 of 19 undehydrated silica gel (Davison 948) which conta~ns 8.10 wt.X
water.
21 Example 8 22 The procedure of Example 7 was fol10wed with the exception 23 that the undehyt~rated silica gel ~Dav~son 948) contalned 8.28 wt.X
24 water.
Ex~mple 9 26 The procedure of Example 7 was followed w1th the exception 27 that the undehydrated s~l1ca gel (Dav~son 948) conta~ned 7.69 wt.X
28 water.
29 Example lO
The procedure of Fxample 7 was followed w1th the except~on 31 that the undehydrated s~l k a gel (Davlson 948) conta~ned 7.90 wt.X
32 water.
33 Example 11 34 The procedure of Example 7 Yas followed w1th the exceptlon that the undehydrated s~llca gel SDavison 948~ conta1ned 8.08 ~t.X
36 ~ater and after addlt~on of the s~llca gel to the flask, the 37 m~xture ~as heated to 85C.

13273~

Example 12 2 The procedure of Example 7 was followed w~th the exceptlon that a triethylaluminum/heptane solut~on ~Z5X) ~s charged ~nto a 4 one-liter three-neck flask contain~ng 100 g of undehydrated s~l~ca s gel (Davison 948) wh~ch conta~ns 8.10 wt.X water and 300 ml of 6 heptane.
7 Catalys~_Test A
8 The activity of the catalyst powders of Examples 1 to 12 g were determ~ned at ambient temperature and 5 ps~g ethylene pressure by the following procedure. A 125 mlllillter v~al was freshly 11 cleaned, heated to 130C for 6 hours, cooled to room temperature 12 and flushed with nitrogen for 10 m~nutes. The vial was provided 13 w~th a magnetic stirr~ng bar and 5 grams of catalyst compos~tion 14 was charged into the v~al. At ambient temperature ethylene gas at 5 psig was fed 1nto the v~al. Polymerization of the ethylene was 16 allowed to proceed for one hour. The y~eld of polyethylene 17 obtalned ~ith each catalyst composit~on ls reported ln Table I.

19 Table l ÇATALYST TEST A_B~ULT

21 Amount 22 Polyethylene 23 Catalys~ Formed~ g 24 Example 1 (Comparat~ve) 5.2 2 5.5 28 5 5.2 29 6 0.1 7 4.4 31 8 4.0 32 9 1.5 2.5 36 ~atalyst Test 3 37 ~he act~vity of the catalyst of Examples 1, 2, and 7 were 38 determlned ln cont~nuous flu~d bed gas phase polymerlzat~on reactor 39 at 300 ps~g total pressure. Ethylene was copo1ymer~zed ~lth hexene-l ln each of these examples.

.

, 1 During the polymerization, ethylene, hexene-l, and 2 nltrogen were cantinuously fed into the reactor to maintain 3 constant gas compositions. Catalyst was injected ~nto the reactor 4 continuously at a rate of 0.5 g/hr to maintain a constant reaction rate. Polymer product was periodically removed from the reactor 6 through a valve to maintain a constant polymer bed high in the 7 reactor.

8 Each of the polymerization reactions was conducted for at 9 least 48 hours to ensure that the product collected was representatlve product produced under the reaction conditions.
11 Table II lists the polymer produced in each example.

14 Temp. C6/C2 Yield MI~ ~ Density 15Catalyst (F) RatiQ g/hr dg/min MIR g/ml 16Example l 185 0.06 300 1.24 18.7 0.923 17 2 l65 0.02 230 0.74 23.4 0.940 18 3 165 0.03 200 0.23 26.8 0.933 19 ~ Melt lndex (MI) and melt lndex ratio (MIR) were determined in accordance with ASTM D-1238.
21 The invention has been described with reference to lts 22 preferred embGdiments. ~rom this description, a person of ordinary 23 skill in the art may appreciate changes that could be made in the 24 invention which do not depart from the scope and spirit of the invention as described above and claimed hereafter.
:`
,' ~' ` :
'

Claims

1. A process for preparing a supported metallocene alumoxane catalyst for gas phase polymerization of olefins, comprising the steps of:
(a) adding undehydrated silica gel to a stirred solution of an aluminum trialkyl in an amount sufficient to provide a mole ratio of aluminum trialkyl to water of from about 3:1 to about 1:2 and allowing the mixture to react;
(b) adding a metallocene to the reacted mixture;
(c) removing the solvent;
(d) drying the solids to a free flowing powder.

2. The process of claim 1, wherein said undehydrated silica gel has a water content of from about 6 to about 10 weight percent.

3. The process of claim 2, wherein the mole ratio of aluminum to transition metal in said metallocene is from about 1000:1 to about 1:1.

4. The process of claim 2, wherein said undehydrated silica gel has a water content of from about 7 to about 9 weight percent and the mole ratio of aluminum trialkyl to water is from about 1.2:1 to about 0.9:1.

5. The process of claim 4, wherein the mole ratio of aluminum to transition metal in said metallocene is from about 300:1 to about 10:1.

6. The process of claim 5, wherein the aluminum trialkyl is trimethyl aluminum or triethyl aluminum.

7. The process of claim 6, wherein said undehydrated silica gel has a water content of from about 7.5 to about 8.5 weight percent.

8. The process of claim 7, wherein said undehydrated silica gel has a surface area of from about 200 to about 400 m2/g, a pore volume of from about l to about 2 cc/g and a particle size of from about 30µ to about 60µ.

9. The process of claim 8, wherein the mole ratio of aluminum to transition metal in said metallocene is from about 150:1 to about 30:1.

10. The process of claim 9, wherein said solids are dried at a temperature of from about 75°C. to about 85°C.

11. A process for preparing a supported metallocene alumoxane catalyst for gas polymerization of ethylene and alpha olefin monomers, comprising the steps of:
(a) adding undehydrated silica gel to a stirred solution of an aluminum trialkyl in an amount sufficient to provide a mole ratio of aluminum trialkyl to water of from about 3:1 to about 1:2 and allowing the mixture to react;
(b) adding to the reaction mixture a metallocene of the formula: (Cp)mMRnXq wherein Cp is a cyclopentadienyl ring, M is a Group 4b or 5b transition metal, R is a hydrocarbyl group of hydrocarboxy group having from 1 to 20 carbon atoms, X is a halogen, and m is a whole number from 1 to 3, n is a whole number from 0 to 3, and q is a whole number from 0 to 3;
(C5R'k)gR"s(C5R'k)MQ3-g, or R"5(C5R'k)2MQ' wherein (C5R'k) is a cyclopentadienyl or substituted cyclopentadienyl, each R' is the same or different and is hydrogen or a hydrocarbyl radical containing from 1 to 20 carbon atoms, a silicon-containing hydrocarbyl radical, or a hydrocarbyl radical wherein two carbon atoms are joined together to form a C4-C6 rings, R" is C1-C4 alkyene radical, a dialkyl germanium or silicone, or an alkyl phosphine or amine radical bridging two (C5R'k) rings, Q is a hydrocarbyl radical having 1-20 carbon atoms, hydrocarboxy radical having 1-20 carbon atoms or halogen and can be the same or different, Q' is an alkylidene radical having from 1 to about 20 carbon atoms, s is 0 to 1, g is 0, 1 or 2; when 9 is 0, s is 0; k is 4 when s is 1 and k is 5 when s is O and M is as defined above;
(c) removing the solvent;
(d) drying the solids to a free flowing powder.

12. The process of claim 11 wherein said metallocene is zirconocene or titanocene.

13. The process of claim 12, wherein said zirconocene is selected from the group consisting of cyclopentadienyl zirconium trichloride; pentamethylcyclopentadienyl zirconium trichloride;
bis(cyclopentadienyl)zirconium diphenyl;
bis(cyclopentadienyl)zirconium dichloride; alkyl substituted cyclopentadienes, and their dihalide complexes; dialkyl, trialkyl, tetra-alkyl, and penta-alkyl cyclopentadienes, and their dihalide complexes; and silicone, phosphorus, and carbon bridged cyclopentadiene complexes.

14. The process of claim 12, wherein said titanocene is selected from the group consisting of monocyclopentadienyl titanocenes; bis(cyclopentadienyl) titanium diphenyl; carbenes represented by the formula Cp2Ti=CH2 ? Al(CH3)2Cl and their derivatives, wherein Cp is a cyclopentadienyl or substituted cyclopentadienyl radical; substituted bis(Cp)Ti(IV) compounds and their dihalide complexes; dialkyl, trialkyl, tetra-alkyl and penta-alkyl cyclopentadienyl titanium compounds and their dihalide complexes; and silicone, phosphine, amine or carbon bridged cyelopentadiene complexes, and thelr dihalide complexes.

15. The process of claim 12, wherein said undehydrated silica gel has a water content of from about 7 to about 9 weight percent and the mole ratio of aluminum trialkyl to water is from about 1.2:1 to about 0.9:1.

16. The process of claim 15, wherein the mole ratio of aluminum to transition metal in said metallocene is from about 300:1 to about 10:1.

17. The process of claim 16, wherein the aluminum trialkyl is trimethyl aluminum or triethyl aluminum.

18. The process of claim 17, wherein said undehydrated silica gel has a water content of from about 7.5 to about 8.5 weight percent.

19. The process of claim 18, wherein said undehydrated silica gel has a surface area of from about 200 to about 400 m2/g, a pore volume of from about 1 to about 2 cc/g and a particle size of from about 30µ to about 60µ.

20. The process of claim 19, wherein the mole ratio of aluminum to transition metal in said metallocene is from about 150:1 to about 30:1.