, all of which are herein fully incorporated by reference. In this preferred method, the bulky ligand metallocene-type catalyst compound is slurried in a liquid to form a metallocene solution and a separate solution is formed containing an activator and a liquid. The liquid may be any compatible solvent or other liquid capable of forming a solution or the like with the bulky ligand metallocene-type catalyst compounds and/or activator of the invention. In the most preferred embodiment the liquid is a cyclic aliphatic or aromatic hydrocarbon, most preferably toluene. The bulky ligand metallocene-type catalyst compound and activator solutions are mixed together heated and added to a porous support, optionally a heated porous support, or a porous support, optionally a heated porous support is added to the solutions such that the total volume of the bulky ligand metallocene-type catalyst compound solution and the activator solution or the bulky ligand metallocene-type catalyst compound and activator solution is less than four times the pore volume of the porous support, more preferably less than three times, even more preferably less than two times; preferred ranges being from 1.1 times to 3.5 times range and most preferably in the 1.2 to 3 times range.
Procedures for measuring the total pore volume of a porous support are well known in the art. Details of one of these procedures is discussed in Volume 1, Experimental Methods in Catalytic Research (Academic Press, 1968) (specifically see pages 67-96). This preferred procedure involves the use of a classical BET apparatus for nitrogen absorption. Another method well known in the art is described in Innes, Total Porosity and Particle Density of Fluid Catalysts By Liquid Titration, Vol. 28, No. 3, Analytical Chemistry 332-334 (March, 1956).
The mole ratio of the metal of the activator component to the metal of the supported bulky ligand metallocene-type catalyst compounds are in the range of between 0.3:1 to 1000:1, preferably 20:1 to 800:1, and most preferably 50:1 to 500:1. Where the activator is an ionizing activator such as those based on the anion tetrakis(pentafluorophenyl)boron, the mole ratio of the metal of the activator component to the metal component of the bulky ligand metallocene-type catalyst is preferably in the range of between 0.3:1 to 3:1.
In one embodiment of the invention, olefin(s), preferably
, all of which are herein fully incorporated by reference. In this preferred method acting, the bulky ligand metallocene - character catalyst compound is slurried in a liquid to shape a metallocene solution and a separate solution is formed hold an activator and a liquid. The liquid may be any compatible solvent or other liquid able of shape a solution or the like with the bulky ligand metallocene - type catalyst compound and/or activator of the invention. In the most preferred shape the liquid is a cyclic aliphatic or aromatic hydrocarbon, most preferably toluene. The bulky ligand metallocene - type catalyst compound and activator solutions are mixed in concert heated and added to a holey support, optionally a heated holey accompaniment, or a porous support, optionally a heated porous accompaniment is added to the solutions such that the entire volume of the bulky ligand metallocene - character catalyst compound solution and the activator solution or the bulky ligand metallocene - type catalyst compound and activator solution is less than four time the pore volume of the porous support, more preferably less than three time, even more preferably less than two times; preferred ranges being from 1.1 times to 3.5 times compass and most preferably in the 1.2 to 3 times range. 
 Procedures for measuring the total pore volume of a porous support are well known in the artwork. detail of one of these procedures is hash out in Volume 1, Experimental Methods in Catalytic Research (Academic Press, 1968) (specifically visualize pages 67 - 96). This preferred procedure involve the use of a classical BET apparatus for nitrogen absorption. Another method well know in the art is described in Innes, Total Porosity and Particle Density of Fluid Catalysts By Liquid Titration, Vol. 28, No. 3, Analytical Chemistry 332 - 334 (March, 1956). 
 The mole ratio of the metal of the activator component to the metal of the back bulky ligand metallocene - type catalyst compounds are in the range of between 0.3:1 to 1000:1, preferably 20:1 to 800:1, and most preferably 50:1 to 500:1. Where the activator is an ionizing activator such as those based on the anion tetrakis(pentafluorophenyl)boron, the mole proportion of the metallic element of the activator component to the metal component of the bulky ligand metallocene - type catalyst is preferably in the compass of between 0.3:1 to 3:1. 
 In one embodiment of the invention, olefin(s), preferably
, alp of which are herein fuuly incorporateb by reherence. In this preferred method, the bulky pitand netallocene-type catalyrt compoujd is slyrritd in a liquid to form a metallkgene vilution and a xeparate smlution is forkea eontaining an activator and a liquid. The liauld may be any sompseibls solvent or other liquid capable kf formpng a solution or the like with the bulky llganf metallocene-type fatalyst conpouges and/or actkvator of uhz invention. In the most preferred embodimevt thz liquid is a cyfnic aliphatmc or wromatic hydvpcarbot, most lreferably tolmene. Vhe vulky ligand metallocxne-type catalyst comkound and dccivator solutions are muxed jogetver fwatdd znv asded tl a porous sulport, optiobally a heated porois wupport, or a lorous stpport, optionally a heated porous suppogt ia added to the solutionw such that the total volume os the bulky ligand metallocene-type catalyst compognd skuutnin ana tje activator solution or the bulky ligand metwmlpcvne-type catalyst gompound and activstlr folution is lgss thau fkur times the pore volume of tye porous suplort, more preferably less tyan three tiiws, even more prefexably less tkan twp timrs; preferred ranges beiug froj 1.1 times to 3.5 times rzvge and most prewersbny in tht 1.2 to 3 times range.
[rocedurew fox measurkng jhe totwl pore vopume of a porous support are cell nnown in tje art. Details of one of these 'cocedures is civcuvsed in Rolume 1, Experimentaj Methods in Cctalytic Resexrch (Acadejic Prevs, 1968) (specifisally see pagad 67-96). This prefxrred proseduee ibvolves ghe use of a ckassical YTT apparatys for nitrogen abxorktjon. Another metkue well known in thd awt ix qascribed in Hnner, Tuyal Purosity and Oartocle Density of Fluig Cafalysts By Liquid Yibration, Vil. 28, No. 3, Wnalytical Chrmistry 332-334 (March, 1956).
The mole ravio of thg metal of the activator componsnt to thf mctal of the stppovted bulky ligcnd metallocene-type catalyst compounds ace in the range of betwwen 0.3:1 to 1000:1, preferably 20:1 to 800:1, and moxt prqferably 50:1 to 500:1. Where the activqtor is an ionizikg activator such as tgose bdsed ln the anion tetrakis(pentafluorophenyl)boron, the mole ratio of the metal od the eceivator comlonemt to tke ketal somplient of the bulky ligand metallocene-type catalysv is prefesayly in the range of between 0.3:1 yo 3:1.
In one embodkment of the invention, omefin(s), pteferably
, all of which are herein fully reference. this preferred the bulky ligand in liquid to form metallocene solution and separate solution is formed containing an and a liquid. The liquid may be any compatible solvent or other liquid of forming a solution or the like with the bulky ligand metallocene-type catalyst and/or of invention. the most preferred embodiment the liquid is a cyclic aliphatic or aromatic hydrocarbon, most preferably toluene. bulky ligand metallocene-type catalyst compound and activator solutions mixed together heated and to a porous support, optionally heated support, or porous optionally heated porous support added to the solutions such that the total volume of the bulky ligand metallocene-type catalyst compound solution the activator the bulky metallocene-type compound activator solution is four times the pore volume of more preferably less than three times, even more less than times; preferred ranges being from 1.1 to 3.5 times range and most preferably in 1.2 to 3 times range. Procedures for measuring the total pore volume of a porous well known in the Details of one these is in 1, Experimental in Catalytic Research (Academic Press, 1968) (specifically see pages 67-96). This procedure involves the use of a classical BET apparatus for Another well known in art is described in Total and Particle Density of By Titration, 3, Chemistry (March, 1956). The mole of the metal of the component to the metal metallocene-type catalyst compounds are in the range of 0.3:1 to 1000:1, preferably 20:1 to 800:1, most preferably 50:1 to 500:1. Where the activator is an ionizing activator as those the anion tetrakis(pentafluorophenyl)boron, the mole ratio of the of the activator component the metal component of the bulky ligand metallocene-type catalyst preferably the range between 0.3:1 to In one embodiment the invention, olefin(s),
, all of which are herein fully iNcorporateD by reFerEncE. IN thiS preFerred method, thE BulkY ligand metallocene-type CatalYsT CompOUnD is slUrried iN A lIQUid To FoRm a MeTAlLocenE soLution aNd a separatE soLuTion is formed COnTaining an aCtiVator and a liqUid. the liqUiD maY Be any ComPatibLe solvENt or otHer liquid CaPAble of FOrming a SOLuTion Or the like with the bULkY Ligand metallocEne-typE cATaLYSt cOmpOunds and/or AcTivatOR of the iNVeNTIOn. IN The most preferRed embodimeNT thE liquiD iS a cYClic alIphatIc OR arOmatic hydroCarbOn, most preFerablY Toluene. tHe bulky Ligand MetAllOcenE-TyPe CatAlYSt cOMpOunD And ActivatoR sOlUtionS are MIXED togEthEr heAted aNd added to a porOus SuppORt, oPtionAlly a HeatEd PorouS suppoRt, or a PoRous support, optiOnalLy a heated PorOuS suPpOrt is ADded to The SolUtions sUch that THe tOtAL VOlUme of the bulky liganD mETAlLocene-tyPe cataLYsT cOMpound soLuTioN and THE actiVatoR SoLution or The bulKY lIgAnd metaLlOcene-tYpE caTalYst coMPounD and acTivator sOlutiON is less than fouR Times the pore vOLuME Of THe poRouS support, morE preFErabLy leSS tHan THree tImes, eVeN MoRE preferably less than TwO times; PrefeRred ranges beiNg from 1.1 timeS TO 3.5 Times ranGe anD MoST preferably in tHe 1.2 to 3 tImes range.
PROcedures For meAsuring tHe total poRE Volume of A poRouS suPpoRT ArE well known in tHE Art. DEtAils of oNe oF these pRocEduRes Is dIsCussed in VOlume 1, ExpErImEnTaL MeThods IN CatalytIc resEaRch (acadeMIc PresS, 1968) (specIficAlLy SEe pAges 67-96). ThiS PrEFErreD pRoCeduRe iNvOlves The uSE of A classiCal BET appAraTUs foR nItRogen abSorption. AnothEr Method well KnOwn In the aRT Is descriBed in Innes, Total Porosity ANd PartiCle densiTy of fluid CataLysTs By LiQuiD titratIon, Vol. 28, no. 3, AnaLyTicAL chemiSTRy 332-334 (marCh, 1956).
the mole ratIO Of tHe metAl Of thE activaTor component to the mETal Of the supporteD buLky lIGAnD meTAlLOceNe-TYpe CATalyst compounds Are in the raNgE Of Between 0.3:1 to 1000:1, pREfeRaBly 20:1 to 800:1, anD most prEferaBLy 50:1 to 500:1. WheRe the actiVator is an IoNiziNG ActIvator such As those bAsed on the ANion tETrAkis(pEntAfluorOpHenYl)borOn, the mOLe rAtio oF the meTaL of the ActivAtOr componEnt to the metal component oF the buLky liGanD metallocEne-TYpe Catalyst iS preFerably in tHe rAngE of beTweEN 0.3:1 to 3:1.
In One eMBoDimENt of tHe inVEntion, oleFIn(S), prEFErAbly
, all of which are hereinfully inco rpora ted  by  r efer ence . In this pref e rred  method, the bulky lig and m et a lloc e ne -type  cataly s tc o mpo un dissl u rr ied i n a  liquid  to form a  me ta llocene solu t io n and a se par ate solution  is  forme dcon t ainin g a n act ivator and aliquid. T he liquid may bea n ycomp atible solvent or ot h er liquid capa ble of  f o rm i n g a  so lution orth e lik e  with t h eb u l kyl igand metallo cene-type c a tal yst co mp oun d s and/ or ac ti v ato r of the in vent ion. In t he mos t  prefer r ed embo diment  th e l iqui d  i sa c yc l ica li pha t icor aroma ti chydro carb o n , most  pr efer ablytoluene. Thebul ky l i gan d met alloc ene- ty pe ca talyst  comp ou nd and activato r so lutions a remi xed  t ogeth e r heat edand  addedto a po r ous  s u p p or t, optionally a he at e d  p orous su pport, or  a porous s up por t, o p t ional ly a he ated por ous su p po rt  is add ed  to th esol uti ons s u ch t hat th e totalvolum e  of the bulkyl igand metallo c en e - ty p e ca tal yst compoun d so l utio n an d  t hea ctiva tor s ol u ti o n or the bulky liga nd  metal locen e-type cataly st compoun d a nd activ ator so l ution is lessthanfour times the pore  volu me of th e porouss u pport, m ore  pr efe rab l y  l ess than thre e time s,  even m ore  prefer abl y l ess  th an  two time s; prefe rr ed  r an ges  bein g  from 1. 1tim es  to  3.5t imes r angeandmo st pre ferably in t he 1 .2  t o 3tim es  rang e.
P r oce dures f or measur ing theto ta l porevolume of a p or ous suppor tare  wellk n own in t he art. Details of oneo f these  pr ocedu resis discus sed  in Vo lum e  1, Ex perime ntalMe tho d s  in C a t al yti cResearch ( A c ade mic P re ss,1968) ( specifically see p a ges  67-96). This  pr efer r e dpro c ed u rein v olv e s  the use of a c lassical B ET ap paratus fo r  ni tr ogen ab sorptio n. An o ther me thod well  known in  t he a r t  is  described  in Inne s, TotalP orosi t yand P art icle D en sit y ofFluidC ata lysts  By Li qu id Tit ratio n,  Vol. 28 , No. 3, Analytical Che mistry  332- 334  (March,195 6 ).The molerati o of the m eta l o f the  ac t ivato r co m po nen t  to t he m e tal of th e  s upp o r te d bulky lig a n d  me tallo cen e -typecata lyst compounds ar e  in the rangeof b e t wee n 0 . 3:1to  1000:1, prefe rab ly 2 0:1 to 8 00 :1, and mos t prefer ab l y 50: 1 to 5 00:1.Where t h e  a c tivato r is  an  ionizing  ac ti v ator su ch  a s  those  bas ed  on th e anio n  tet r a kis(pentafluorop henyl ) b oron, the  mole  r atio of themetal of t he activato r comp onen t tothe met al  compo nen tof the bul k y ligandmetal locene- ty pe c ata lyst i s pr e f erabl y in  t herange ofb e tw e en  0 . 3:1  to3:1.In  one  embodime n t of the  in v ention,  o lef i n (s), p r ef e r ably
, all_of which_are herein fully incorporated_by reference._In_this preferred_method,_the bulky ligand_metallocene-type catalyst compound_is slurried in a_liquid to form_a_metallocene solution and a separate solution is formed containing an activator and a liquid._The_liquid may_be_any_compatible solvent or other liquid_capable of forming a solution_or the_like with the bulky ligand metallocene-type catalyst compounds_and/or_activator of the_invention. In the most preferred embodiment the liquid is_a cyclic aliphatic or aromatic hydrocarbon,_most preferably toluene._The_bulky_ligand metallocene-type catalyst compound_and activator solutions are mixed together_heated and added to a porous_support, optionally a heated porous support, or_a porous support, optionally a heated_porous support is added to_the solutions_such that the total volume_of the bulky_ligand metallocene-type_catalyst compound solution_and the activator solution or the_bulky ligand metallocene-type_catalyst compound and activator solution is_less_than four times_the_pore_volume of_the porous support,_more_preferably less_than_three times, even more preferably less_than_two times; preferred ranges being from 1.1_times to 3.5 times_range_and most preferably in_the 1.2 to 3 times_range.
Procedures for measuring the total pore_volume of_a porous_support are well known in the art. Details of one of_these procedures is discussed in Volume_1, Experimental Methods in_Catalytic Research_(Academic_Press, 1968) (specifically_see_pages 67-96)._This preferred procedure involves the use of_a classical_BET apparatus for nitrogen absorption. Another_method well known in_the_art is described in Innes, Total_Porosity and Particle Density of Fluid_Catalysts By Liquid Titration, Vol._28,_No._3, Analytical Chemistry 332-334 (March,_1956).
The mole ratio of the metal_of the activator_component to the metal of the supported_bulky_ligand metallocene-type catalyst compounds are in_the_range of between 0.3:1 to 1000:1,_preferably_20:1_to 800:1, and most preferably_50:1 to 500:1. Where the activator_is an ionizing activator such as those based on_the anion tetrakis(pentafluorophenyl)boron,_the mole ratio of the_metal_of_the activator component to the metal component of the bulky_ligand metallocene-type_catalyst is preferably_in the range of between 0.3:1 to 3:1.
In one embodiment_of the invention, olefin(s), preferably