A Theoretical Investigation of the Structure and Function of MAO Methylaluminoxane - PowerPoint PPT Presentation

1 / 32
About This Presentation
Title:

A Theoretical Investigation of the Structure and Function of MAO Methylaluminoxane

Description:

A Theoretical Investigation of the Structure and Function of MAO (Methylaluminoxane) ... Structural Investigation. Constructing the Cages. Schlegel Diagram. 3 ... – PowerPoint PPT presentation

Number of Views:220
Avg rating:3.0/5.0
Slides: 33
Provided by: zieglerres
Category:

less

Transcript and Presenter's Notes

Title: A Theoretical Investigation of the Structure and Function of MAO Methylaluminoxane


1
  • A Theoretical Investigation of the Structure and
    Function of MAO (Methylaluminoxane)

Eva Zurek, University of Calgary
2
Computational Details
  • DFT Calculations performed with ADF 2.3.3 and
    2000
  • Functional LDA along with gradient corrected
    exchange functional of Becke correlation
    functional of Perdew
  • Basis-set double-z STO basis with one
    polarization function for H, C, Al, O triple-z
    STO basis with one polarization function for Zr
  • Frequencies single-point numerical
    differentiation
  • Molecular Mechanics UFF2 parameterized to give
    entropies/enthalpies which agreed with those
    obtained from ADF
  • Solvation COnductor-like Screening Model
    (COSMO)
  • NMR Chemical Shifts triple-z 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

3
Catalysis
  • K. Ziegler (1953) G. Natta (1954) Nobel Prize
    in 1963
  • Annual production of polyolefins is a hundred
    million tons (2001)
  • 1/3 of the polymers made today are by
    Ziegler/Natta catalysis
  • Polyethylene is the most popular plastic in the
    world
  • Grocery bags, shampoo bottles, childrens toys,
    bullet proof vests (Kevlar),
  • Goal to control MW, stereochemistry
  • Single site catalysts narrow MW distribution
    higher stereoselectivity higher activity
  • Allow detailed structural mechanistic studies

4
Single-Site Homogeneous Catalysis
  • Catalysts L1L2MR1R2 LCp, NPR3, NCR2 MTi,
    Zr, Rmethyl, propyl, etc.
  • Co-Catalyst (Anion) B(C6F5)3, MAO
    (Methylaluminoxane)
  • MAO Cp2Zr(CH3)2 ? Cp2ZrCH3 MAOMe-

5
MAO is a Black Box
MAO is formed from controlled hydrolysis of TMA
(trimethylaluminum)
Why is an excess of MAO necessary for
polymerization? (Al/Zr gt 1000)
Does not crystallize
Gives complicated NMR
Industrially, one of the most important
co-catalysts
6
Pure MAO
  • presence of different oligomers and multiple
    equilibria
  • (AlOMe)x ? (AlOMe)y ? (AlOMe)z
  • Experimental data suggests that x,y,z range
    between 9-30 14-20

7
Structural Investigation
  • Three-dimensional cage structures, consisting of
    square, hexagonal and octagonal faces
  • Four-coordinate Al centers bridged by
    three-coordinate O atoms
  • MeAlOn, where n ranges between 4-16
  • ADF calculations were performed on 35 different
    structures

8
Constructing the Cages
3-D Representation
Schlegel Diagram
9
MAO Cage Energies
  • The order of stability is, 3H gt 2HS gt HOS gt
    2OS gt 2HO gt 2SH gt 2SO gt 3S gt 2OH
  • Structures composed of square and hexagonal faces
    only have the lowest energies for a given n
  • SF OF 6

-2 octagonal 8 square faces -16 atoms (2SO)
-Energy -6037.87kcal/mol
-2 octagonal 8 square faces -4 (3S) 8 (2SO) 4
(2OS) -Energy -6028.60kcal/mol
-4 hexagonal 6 square faces -8 (2SH) 8
(2HS) -Energy -6070.48kcal/mol
10
Entropies Enthalpies
  • UFF2 (Universal Force Field) parametrized for
    (AlOMe)4 and (AlOMe)6
  • Tested on two different (AlOMe)8 oligomers
  • ZPE differs by up to 1.27 kcal/mol entropy by up
    to 1.39 kcal/mol (298.15K)

11
Gibbs Free Energy per (AlOMe) Unit
12
Percent Distribution
average unit formula of (AlOMe)18.41,
(AlOMe)17.23 , (AlOMe)16.89, (AlOMe)15.72 at
198K, 298K, 398K and 598K
13
Real MAO
  • Free TMA ((AlMe3)2) is always present in a MAO
    solution
  • TMA and pure MAO react with each other
    according to the following equilibrium
  • (AlOMe)n m/2(TMA)2? (AlOMe)n(TMA)m
  • Difficult to measure amount of bound TMA.
    Estimates give Me/Al of 1.4 1.5

14
Reactive Sites in MAO
15
(No Transcript)
16
Equilibrium Including TMA (1mol/L)
  • Most abundant species at every temperature still
    (AlOMe)12
  • Increasing temperature shifts equilibrium towards
    slightly smaller structures
  • Experimentally obtained ratio of Me/Al 1.4 or
    1.5 not obtained

17
Interaction Between MAO, TMA and THF
-14.17kcal/mol
-6.56kcal/mol
-23.15kcal/mol
18
Reactive MAO Cages
19
Real MAO and Cp2ZrMe2
  • Species III heterodinuclear complex contact
    ion pairs/similar separated ion pairs (possibly
    active)
  • Species I a weak complex
  • Species II binuclear complex contact ion-pair
  • Species IV unsymmetrically Me-bridged complex
    (possibly dormant)

20
Testing the Method
Chemical Shifts, ppm
Chemical Shifts, ppm
21
The Weakly Interacting Species
Chemical Shifts, ppm
22
The Active Species
Chemical Shifts, ppm
23
The Dormant Species
Chemical Shifts, ppm
24
Formation of Dormant, Active Species
25
Possible Mechanisms
Dissociative Mechanism
Associative Mechanism
26
First Insertion Dormant Species
Cis-Attack
Zr-O 3.658
Zr-O 3.336
Transition State DEgas 38.80 kcal/mol DEtoluene
35.55 kcal/mol
p-complex DEgas 31.88 kcal/mol DEtoluene 28.43
kcal/mol
Trans-Attack
Zr-O 4.539
Zr-O 4.209
Transition State DEgas 35.37 kcal/mol DEtoluene
29.26 kcal/mol
p-complex DEgas 34.65 kcal/mol DEtoluene 26.96
kcal/mol
27
First Insertion Active Species
Zr-Me 3.938
Zr-Me 2.501
Transition State DEgas 16.63 kcal/mol DEtoluene
18.36 kcal/mol
p-complex DEgas 14.97 kcal/mol DEtoluene 12.32
kcal/mol
Cis-Attack
Zr-Me 3.999
Zr-Me 4.108
p-complex DEgas 20.73 kcal/mol DEtoluene 16.22
kcal/mol
Transition State DEgas 21.87 kcal/mol DEtoluene
17.00 kcal/mol
Trans-Attack
28
Second Insertion Active Species
Zr-Me 2.517
Transition State DEgas 22.29 kcal/mol DEtoluene
24.11 kcal/mol
p-complex DEgas 14.77 kcal/mol DEtoluene 9.13
kcal/mol
Zr-Me4.658
Transition State DEgas 21.26kcal/mol DEtoluene
16.40 kcal/mol
29
Second Insertion Active Species
Zr-Me 4.161
p-complex DEgas 18.70 kcal/mol DEtoluene 13.69
kcal/mol
(AlOMe)6(TMA)(Cp2ZrMeProp) C2H4 Trans Attack
a - agostic Interactions Insertion Profile
30
Why is an Excess of MAO Necessary?
  • 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
  • Cp2ZrMeMeMAO- is dormant
  • Cp2ZrMeAlMe3MeMAO- is active
  • The same feature which makes a cage structure
    less stable is the same that makes it
    catalytically active!!!

31
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
  • Basic impurities in MAO can influence the
    equilibrium
  • 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
  • First insertion trans-approach has lower
    insertion barrier
  • Second insertion trans-approach, a-agostic
    interaction has no insertion barrier. An uptake
    barrier needs to be found

32
Miscellaneous
  • Future Work
  • - to finish calculating uptake insertion
    barriers for the second insertion examine
    termination barriers. Do the anion cation
    associate after insertion?
  • Acknowledgements
  • - Tim Firman, Tom Woo, Robert Cook, Kumar
    Vanka, Artur Michalak, Michael Seth, Hans Martin
    Senn and other members of the Ziegler Research
    Group for their help and fruitful discussions
  • - Dr. Clark Landis, University of Wisconsin
    for giving us UFF2
  • - Novacor Research and Technology (NRTC) of
    Calgary ()
  • - NSERC ()
  • - Alberta Ingenuity Fund ()
Write a Comment
User Comments (0)
About PowerShow.com