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A Theoretical Investigation of the Dormant & Active Species in MAO (Methylaluminoxane)- Activated, Cp 2 ZrMe 2 -Catalyzed Olefin Polymerization Eva Zurek, Tom Ziegler*, University of Calgary
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Computational Details DFT Calculations: performed with ADF (Amsterdam Density Functional) 2.3.3 and 2000. Functional: LDA along with gradient corrected exchange functional of Becke; correlation functional of Perdew. Basis-set: double- STO basis with one polarization function for H, C, Al, O; triple- STO basis with one polarization function for Zr. Solvation: COnductor-like Screening Model (COSMO). NMR Chemical Shifts: triple- STO basis with two polarization functions for H and C; Gauge Including Atomic Orbitals (GIAO). Transition States: geometry optimizations along a fixed reaction coordinate. TS where gradient less than convergence criteria. For insertion barriers this is C -C ethylene distance.
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Single-Site Homogeneous Catalysis Catalysts: L 1 L 2 MR 1 R 2 ; L=Cp, NPR 3, NCR 2 ; M=Ti, Zr, R=methyl, propyl, etc. Co-Catalyst (Anion): B(C 6 F 5 ) 3, MAO (Methylaluminoxane) MAO + Cp 2 Zr(CH 3 ) 2 Cp 2 ZrCH 3 + + MAOMe -
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MAO Does not crystallize Gives complicated NMR Industrially, one of the most important co-catalysts MAO is formed from controlled hydrolysis of TMA (trimethylaluminum) Why is an excess of MAO necessary for polymerization? (Al/Zr > 1000) MAO is a ‘Black Box’
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‘Pure MAO’ Percent Distribution average unit formula of (AlOMe) 18.41, (AlOMe) 17.23, (AlOMe) 16.89, (AlOMe) 15.72 at 198K, 298K, 398K and 598K
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‘Real’ (TMA-Containing) MAO
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Reactive (R-MAO) MAO Cages R-MAO: 5.97% R-MAO+TMA: 6.13%
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Species I: a weak complex Species II: binuclear complex contact ion-pair Species III: heterodinuclear complex contact ion pairs/similar separated ion pairs (possibly active) Species IV: unsymmetrically Me-bridged complex (possibly dormant) ‘Real’ MAO and Cp 2 ZrMe 2
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Testing the Method Chemical Shifts, ppm
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The Weakly Interacting Species Chemical Shifts, ppm
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The ‘Active’ Species Chemical Shifts, ppm
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The ‘Dormant’ Species Chemical Shifts, ppm
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First Insertion: ‘Dormant’ Species Cis-Attack Trans-Attack Zr-O: 4.209 Zr-O: 3.336 Transition State E gas = 38.80 kcal/mol E toluene = 35.55 kcal/mol Transition State E gas = 35.37 kcal/mol E toluene = 29.26 kcal/mol
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First Insertion: ‘Active’ Species Cis-Attack Trans-Attack Zr-Me: 4.108 Transition State E gas = 21.87 kcal/mol E toluene = 17.00 kcal/mol Transition State E gas = 16.63 kcal/mol E toluene = 18.36 kcal/mol Zr-Me: 2.501
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Second Insertion: Trans TS Transition State E gas = 22.29 kcal/mol E toluene = 24.11 kcal/mol Transition State E gas = 21.26kcal/mol E toluene = 16.40 kcal/mol Zr-Me: 2.517ÅZr-Me:4.658Å -complex E gas = 18.70 kcal/mol E toluene = 13.69 kcal/mol
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Second Insertion: Cis TS Zr-Me: 2.503Å Transition State E gas = 16.39 kcal/mol E toluene = 18.25 kcal/mol Transition State E gas = 21.81kcal/mol E toluene = 16.85 kcal/mol Zr-Me:4.925Å Transition State E gas = 20.05 kcal/mol E toluene = 14.90 kcal/mol Zr-Me:4.089Å
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In order for polymerization to occur, an excess of MAO is needed (typical conditions Al/Zr 1000 - 10,000) Most stable ‘pure’ MAO species do not contain strained acidic bonds and therefore do not react with TMA For example, (AlOMe) 12, ~19% at 298.15 K [Cp 2 ZrMe] + [MeMAO] - is dormant [Cp 2 ZrMe] + [AlMe 3 MeMAO] - is active The same feature which makes a cage structure less stable is the same that makes it catalytically active!!! Why is an Excess of MAO Necessary?
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Conclusions MAO consists of 3D cage structures with square and hexagonal faces Very little TMA is bound to ‘pure’ MAO; most exists as the dimer in solution Identified most likely structures for ‘dormant’ and ‘active’ species in polymerization First insertion: - cis-approach has an associated TS; trans-approach has a dissociated TS - trans-approach has lower insertion barrier Second insertion: - trans-approach, -agostic interaction has no insertion barrier. An uptake barrier needs to be found - cis-approach, lowest barrier for TS with -agostic bond (14.90 kcal/mol)
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Future Work: - to finish calculating uptake & insertion barriers for the second insertion; examine termination barriers. Acknowledgements: - Robert Cook, Kumar Vanka, Artur Michalak, Michael Seth, Hans Martin Senn, Zhitao Xu and other members of the Ziegler Research Group for their help and fruitful discussions - Novacor Research and Technology (NRTC) of Calgary ($$$) - NSERC ($$$) - Alberta Ingenuity Fund ($$$) Miscellaneous
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