Late Transition Metal and Aluminium Complexes for the Polymerization of Ethene and Acrylates

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Late Transition Metal and Aluminum Complexes for the Polymerization of Ethene and Acrylates Katariina Yliheikkilä Laboratory of Inorganic Chemistry Department of Chemistry Faculty of Science University of Helsinki Finland Academic Dissertation To be presented, with the permission of the Faculty of Science of the University of Helsinki, for public criticism in Auditorium A129 of the Department of Chemistry, A. I. Virtasen Aukio 1, on November 25 th 2006 at 12 o’clock noon. Helsinki 2006

Transcript of Late Transition Metal and Aluminium Complexes for the Polymerization of Ethene and Acrylates

Late Transition Metal and Aluminum Complexes for the Polymerization of Ethene and Acrylates

Katariina Yliheikkilä

Laboratory of Inorganic Chemistry

Department of Chemistry Faculty of Science

University of Helsinki Finland

Academic Dissertation

To be presented, with the permission of the Faculty of Science of the University of Helsinki, for public criticism in Auditorium A129 of the Department of Chemistry, A. I. Virtasen Aukio 1, on November 25th 2006 at 12 o’clock noon. Helsinki 2006

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Supervisors Professor Markku Leskelä and Docent Timo Repo Laboratory of Inorganic Chemistry Department of Chemistry University of Helsinki Finland Reviewers Professor George J. P. Britovsek Department of Chemistry Imperial College of Science, Technology& Medicine London Professor Tuula Pakkanen Department of Chemistry University of Joensuu Finland Opponent Professor Jouni Pursiainen Laboratory of Physical Chemistry Department of Chemistry University of Oulu Finland ©Katariina Yliheikkilä 2006 ISBN 952-91-1335-2 (paperback) ISBN 952-10-3551-X (PDF) http://ethesis.helsinki.fi Helsinki University Printing House Helsinki 2006

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Abstract Polyethene, polyacrylates and polymethyl acrylates are versatile materials that

find wide variety of applications in several areas. Therefore, polymerization of ethene,

acrylates and methacrylates has achieved a lot attention during past years. Numbers of

metal catalysts have been introduced in order to control the polymerization and to

produce tailored polymer structures. Herein an overview on the possible polymerization

pathways for ethene, acrylates and methacrylates is presented.

In this thesis iron(II) and cobalt(II) complexes bearing tri- and tetradentate

nitrogen ligands were synthesized and studied in the polymerization of tertbutyl acrylate

(tBA) and methyl methacrylate (MMA). Complexes are activated with

methylaluminoxane (MAO) before they form active combinations for polymerization

reactions. The effect of reaction conditions, i.e. monomer concentration, reaction time,

temperature, MAO to metal ratio, on activity and polymer properties were investigated.

The described polymerization system enables mild reaction conditions, the possibility to

tailor molar mass of the produced polymers and provides good control over the

polymerization. Moreover, the polymerization of MMA in the presence of iron(II)

complex with tetradentate nitrogen ligands under conditions of atom transfer radical

polymerization (ATRP) was studied.

Several manganese(II) complexes were studied in the ethene polymerization with

combinatorial methods and new active catalysts were found. These complexes were also

studied in acrylate and methacrylate polymerizations after MAO activation and converted

into the corresponding alkyl (methyl or benzyl) derivatives.

Combinatorial methods were introduced to discover aluminum alkyl complexes

for the polymerization of acrylates and methacrylates. Various combinations of

aluminum alkyls and ligands, including phosphines, salicylaldimines and nitrogen donor

ligands, were prepared in situ and utilized to initiate the polymerization of tBA.

Phosphine ligands were found to be the most active and the polymerization MMA was

studied with these active combinations. In addition, a plausible polymerization

mechanism for MMA based on ESI-MS, 1H and 13C NMR is proposed.

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Preface The experimental part of this thesis was carried out between 2002 and 2006 in the

Laboratory of Inorganic Chemistry, University of Helsinki.

I am most grateful to my supervisors Professor Markku Leskelä and Docent Timo

Repo for their guidance and continuous support during the course of this work. I would

like also to acknowledge Professor Adnan Abu-Surrah, Hashemite University, Jordan, for

his advice.

The Laboratory of Inorganic Chemistry has proved to be an inspiring working

atmosphere and, especially, I want to thank my colleagues at the CatLab for their

supportive attitude. Special thanks to Dr. Kristian Lappalainen, Mikko Lankinen, Dr.

Kirill Axenov, and Minna Räisänen, it has been inspiring and rewarding working with

you!

Docent Martti Klinga and Dr. Mika Polamo are thanked for their help in the

determination of the crystal structures, Eeva Kaija for taking care of the DSC and GPC

measurements, and Sirpa Pirttiperä for her assistance in printing the thesis.

I want to thank my sisters’ in law and their families for friendship and enjoyable

holidays. Special thanks to Paula and Stu for their expertise in revising the language. My

warmest thanks to my parents Rauha and Kalevi, and my parents-in-law Kyllikki and Esa

for their encouragement and continuous support. I would like to express my deepest

gratitude to my husband Janne, and to our daughters Liina and Kerttu for their love,

patience and endless understanding. Without your support this would not have been

possible.

Financial support from the Academy of Finland (Centre of Excellence, Bio- and

Nanopolymer Research Group, 77317), the Finnish Technology Development Agency

(Tekes) and Gust. Komppa foundation is gratefully acknowledged.

Mäntsälä, September 2006

Katariina Yliheikkilä

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List of Original Publications This thesis is based on the following original publications, which are referred to in the

text by Roman numerals I-V.

I Khalid Ibrahim, Katariina Yliheikkilä, Adnan Abu-Surrah, Barbro Löfgren, Kristian

Lappalainen, Markku Leskelä, Timo Repo, Jukka Seppälä: ‘Polymerization of

methyl methacrylate in the presence of iron(II) complex with tetradentate nitrogen

ligands under conditions of atom transfer radical polymerization’ Eur. Polym. J.

2004, 40, 1095-1104.

II Kristian Lappalainen, Katariina Yliheikkilä, Adnan Abu-Surrah, Mika Polamo,

Markku Leskelä, Timo Repo: ’Nitrogen Ligands Bearing Chiral Bulky Aliphatic

and Aromatic Substituents: Crystal Structure of [CoCl2{2,6-bis[R-(+)-

bornylimino)methyl]pyridine}]’ Z. Anorg. Allg. Chem. 2005, 631, 763-768.

III Katariina Yliheikkilä, Kristian Lappalainen, Pascal M. Castro, Khalid Ibrahim,

Adnan Abu-Surrah, Markku Leskelä, Timo Repo: ‘Polymerization of acrylate

monomers with MAO activated iron(II) and cobalt(II) complexes bearing tri- and

tetradentate nitrogen ligands’ Eur. Polym. J. 2006, 42, 92-100.

IV Katariina Yliheikkilä, Kirill V. Axenov, Minna T. Räisänen, Martti Klinga, Mikko

P. Lankinen, Mika Kettunen, Markku Leskelä, Timo Repo: ‘Manganese(II)

complexes in Ethene Polymerization ’ accepted to Organometallics.

V Katariina Yliheikkilä, Mikko P. Lankinen, Minna T. Räisänen, Antti Pärssinen,

Martti Klinga, Markku Leskelä, Timo Repo: ’Aluminum Alkyl - Phosphine

Catalysts for the Polymerization of Acrylates and Methacrylates’ submitted to

Organometallics.

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Table of Contents Abstract ............................................................................................................................... 3 Preface................................................................................................................................. 4 List of Original Publications............................................................................................... 5 Abbreviations and Symbols ................................................................................................ 7 1 Introduction............................................................................................................. 8 2 Scope of the Thesis ................................................................................................. 8 3 Background............................................................................................................. 9

3.1 Polyethene and Polyacrylates and Their Applications............................................ 9 3.2 Polymerization of Ethene...................................................................................... 10

3.2.1 Homogeneous Late Transition Metal Complexes for the Polymerization of

Ethene ................................................................................................................... 10

3.2.2 Polymerization Mechanism ......................................................................... 12

3.3 Polymerization of Acrylates and Methacrylates .................................................. 14 3.3.1 Radical Polymerization................................................................................ 14

3.3.2 Anionic Polymerization ............................................................................... 17

3.3.3 Group Transfer Polymerization ................................................................... 19

3.3.4 Lanthanide and Early Transition Metal Complexes .................................... 21

3.3.5 Late Transition Metal Complexes................................................................ 22

3.4 Aluminum Complexes as Polymerization Catalysts............................................. 23 3.5 Combinatiorial Approach in the Development of Polymerization Catalyst ......... 25

4 Results and Discussion ......................................................................................... 26 4.1 Experimental in General ....................................................................................... 26 4.2 Synthesis and characterization of Manganese(II), Iron(II) and Cobalt(II) Complexes................................................................................................................... 27 4.3 MAO Activated Manganese(II) Complexes in the Polymerization of Ethene ..... 33 4.4 Manganese(II), Iron(II) and Cobalt(II) Complexes in the Polymerization of Acrylates ..................................................................................................................... 35

4.4.1 Tert-butyl Acrylate....................................................................................... 35

4.4.2 Other Acrylates and Methacrylates.............................................................. 41

4.5 Parallel screening of Aluminum Complexes ........................................................ 42 4.6.1 Tert-butyl Acrylate....................................................................................... 43

4.6.2 Methyl Methacrylate.................................................................................... 48

4.6.3 Proposed Mechanism for Polymerization of MMA..................................... 49

5 Conclusion ............................................................................................................ 52 References and Notes........................................................................................................ 53

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Abbreviations and Symbols acac acetylacetonate AIBN azobisisobutyronitrile ATRP atom transfer radical polymerization Bz benzyl CCT catalytic chain transfer (polymerization) Cp cyclopentadienyl EI electron impact ionization EPR electron paramagnetic reconance ESI electrospray ionization EtOH ethanol Et2O diethyl ether GC gas chromatography GTP group transfer polymerization HDPE high density polyethene HR high resolution IR infrared LDPE low density polyethene m meso dyad contains two adjacent stereocenters of the same configuration MAO methylaluminoxane MA methylacrylate Me methyl MeOH methanol MMA methylmethacrylate MMAO modified methylaluminumoxane MS mass spectrometry MTS 1-methoxy-1-(trimethylsiloxy)-2-methylprop-1-ene MWD molecular weight distribution n-BuLi n-butyllithium NMR nuclear macnetic reconance PE polyethene Ph phenyl r racemic dyad contains two centers of opposing stereochemistries RAFT reversible addition-fragmentation chain transfer RT room temperature (S)-BINAP (S)- (-)-2,2'-Bis(diphenylphosphino)-1'1-binaphthyl SFRP stable free radical mediated polymerization tBA tertbutyl acrylate TEA triethylaluminum TEMPO 2,2,6,6-tetramethyl-1-piperidine N-oxyl (radical scavenger) Tg glass transition temperature THF tetrahydrofuran TIBA triisobutylaluminum Tm melting point temperature TMA trimethylaluminum UV-Vis UV-Visible spectroscopy

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1 Introduction Polymers are important materials of today’s society in many areas and the

demand for polymers has grown enormously over the last sixty years. The success of

polymers is to be found in the unique combination of hardness, lightness, resistance of

corrosion, flame retardant properties, weather resistance, rigidity and toughness. Today

many polymers are produced by reactions which are catalyzed by organometallic

compounds.

Catalytic production of polyolefins started in the mid 1950’s when titanium based

trialkylaluminum activated catalyst were introduced by Karl Ziegler and Giulio Natta.1

The discovery of metallocenes with methylaluminoxane (MAO) as an activator in the

beginning of 1980 is a milestone on the research field of polymerization catalysts.2

Polymerization activity was increased drastically and uniform, tailored polymers were

produced. However, metallocenes based on early transition metals have one drawback

due to their sensitivity against polar functionalities. The search of more tolerant catalyst

system led to an introduction of late transition metal catalysts in 1995.3 Since then the

development in the late transition metal catalyzed polymerization of ethene and polar

monomers has continued and these recent developments are reviewed in Chapter 3.

2 Scope of the Thesis In the beginning of this work it was known that the homopolymerization of

olefins,4 methacrylates and acrylates5 could be carried out with aluminum alkyl activated

late transition metal complexes. In the polymerization of olefins it was observed that

besides the metal, the ligand also has a significant effect on the activity, and the structure

and properties of polymer material produced. This was a starting point for a study of

various nitrogen donor ligands with already known active metals in the polymerization of

acrylates.

Only a little was known about manganese complexes as polymerization catalyst6

though manganese complexes are widely used as catalysts in many other reactions.7 The

question was raised; could manganese complexes work in polymerization if an

appropriate ligand was found? Since there is a limited amount of literature on this topic,

combinatorial chemistry tools were employed to speed up the finding of possible

catalysts.

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A disadvantage of the late transition metal complexes is that the complexes must

be activated with aluminum alkyls to form an active species. This introduced another

interesting question; could it be possible to discover aluminumalkyl complexes that

operate as such without activation in the polymerization of acrylates and methacrylates?

In addition, the purpose of this work was to develop new catalytic systems based

on Mn, Fe, Co and Al complexes in order to afford tailor-made polymers and finally to

achieve a better understanding of the polymerization mechanism of acrylates with

aluminum alkyl complexes bearing phosphine ligands.

3 Background

3.1 Polyethene and Polyacrylates and Their Applications Polyethene (PE) was discovered over 70 years ago and to date it is the most

widely used plastic. The commercial production of PE was over 23 Mtons in 2004, and

the annual growth from the previous year was 5.6%.8 A significant issue in the increased

consumption of polyethene products has been the continuing development in polyethene

properties and polymerization processes. Polyethene is versatile and it possesses

properties such as flexibility, strength, lightness, stability, impermeability and

processability. The list of PE products is extensive, and their applications include, for

example, food and house ware packing and films, gas and plumbing pipes, electrical

cable insulation, toys, car parts and petrol tanks, bullet proof vests, joint and bone

replacements, and waterproof coatings.9

Polyethene is classified based on its density, branching and molecular weight.

These factors strongly influence on the properties of polyethene. In today’s industrial

market low density (LD) PE is produced in high-temperature and high-pressure processes

through free radical polymerization, but in the production of high density (HD) PE the

control over polymerization, i.e. chain branching and length, is unattainable with this

method. Thus, HDPE is produced by chromium/silica catalysts, Ziegler-Natta catalysts

or metallocene catalysts.10 Besides tuning the structure of the product the use of a catalyst

enables mild reaction conditions, hence lowering the production costs.

Acrylate based polymers are utilized in a variety of applications that include

adhesives in coatings and paints,11 contact lenses,12 dental restorations and prostheses.13

Polymethylmethacrylate (PMMA) is used in applications where impact strength and high

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transmittance is needed and it is employed as construction material and in biomedical

application, such as artificial intraocular lenses, dentures and bone cement in the fixation

of prosthetic joints.14 In cosmetic surgery, tiny PMMA microspheres suspended in

collagen solution are injected under the skin to reduce wrinkles or scars permanently.15

The PMMA market is predicted to grow in the future in applications requiring high

optical performance, such as LCD (liquid crystal display) plates. Commercial trade

names of PMMA products are for example commercial Plexiglas®, Perspex®,

Acrylite®, Acrylplast®, and Lucite®.16

The free radical polymerization process is widely used in industry to convert

acrylate monomers rapidly to solid polymer.17 In the initiation radical species attack the

monomer’s vinylic double bond. Radicals for the initiation can be formed by various

methods. Thermal initiators, such as peroxides and azo compounds, decompose to

radicals when heated. Other ways to produce radicals include redox initiators, light

decomposition of the initiator (photo polymerization) or initiation by ionizing radiation.17

The control over molar mass and molar weight distribution is poor in free radical

polymerization due to chain transfer and termination reactions.17 A number of methods to

gain control have emerged in polymerization of acrylates, including controlled radical,

anionic, group transfer and late transition metal mediated polymerization. These methods

are referred in Chapter 3.3.

Hence, the discovery of new catalysts is important in order to continuously

develop and produce tailor made polymer structures for various applications.18 With well-

defined catalytic systems it is possible to understand and control the effects of catalyst

structure on polymer structure and composition, and thus new polymer materials can be

obtained in mild reaction conditions.

The following literature review is focused on the polymerization of ethene and

acrylates and limited to literature relevant to the present study.

3.2 Polymerization of Ethene

3.2.1 Homogeneous Late Transition Metal Complexes for the Polymerization of Ethene In the mid nineties the invention of methylaluminoxane (MAO) activated

homogeneous α-diimine nickel(II) and palladium(II) complexes (Scheme 1) that

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polymerized ethene or higher α-olefins with high activity initiated the intensive research

on the late transition metal complexes in the field of polymerization catalysis.3 By simple

ligand and reaction condition modifications various products were obtained from ethene

with these catalysts.19 Furthermore these catalysts were reported to catalyze

copolymerization of alkenes with alkyl acrylates.3(b),20 Some years later salicylaldiminato

nickel(II) catalysts for the ethene polymerization were reported.21 These catalyst

precursors are activated for example by tris(pentafluorophenyl)borane [B(C6F5)3] and

depending on the catalyst’s structure they are yielding moderately branched or linear

polyethene.21

In 1998, were discovered highly active 2,6-bis(imino)pyridine based iron(II) and

cobalt(II) catalysts (Scheme 1) that produced linear high molar weight polyethene after

activation with MAO.22 By tuning the ligand structure it is possible to produce

polyethene materials from linear α-olefins23 to high molar mass polymers,24 the

microstructure of which can range from linear24 to highly branched.3(a),25 Within this

catalyst family the cobalt complexes are reported to be less active than their iron

counterparts.24,25(b) and aldimine-derivated catalysts are less active as compared to

ketimine analogues.22(b),23(b),24 In addition, ortho substituents of imine aryl groups have

significant effect on the polymerization. The steric bulk of the ortho aryl substituents

retard chain transfer and experiments have confirmed that decreasing the size of these

ortho substituents is resulting in increased activity and decreased molar mass yielding

catalysts for ethene oligomerization.4(b),23,10 Moreover, bis(imino)pyridine iron(II) and

cobalt(II) complexes bearing single ortho substituent on the aryl rings form selective

catalysts for ethene oligomerization to α-olefins.4(b),23,10 With high MAO loadings

bimodal molar weight distributions are observed with these catalysts due to β-hydrogen

transfer and chain transfer to aluminium (Scheme 3).24

Since the early studies of 2,6-bis(imino)pyridine complexes numerous new

complexes and their use in ethene polymerization and oligomerization have been

reported.4(b),10 This type of iron(II) catalysts was also reported to polymerize various

vinylic polar monomers.26 The advantages of these catalysts over other type of catalysts

(e.g., metallocenes and early transition metal catalysts) are facile preparation and

handling, simple tuning of their polymerization activity by ligand architecture

modification and ability to tolerate polar functionalities.4(b),10 Besides the structure of the

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catalyst, MAO concentration, ethene pressure and polymerization temperature affect the

activity and material propreties.

M

R2

N N

R2

R1 R1

(X)n

NR4

N N

R4

R3 R3M(X)n

A B Scheme 1. General structure of α-diimine (A) and 2,6-bis(imino)pyridine (B) complexes.

Despite extensive development in the field of polymerization catalysts, not highly

active polymerization catalysts with manganese metal centre has been described so

far.4(b),6 Only a few recent reports describe the ethylene and propylene polymerization

activity of complexes such as bis(imino)pyridine,27 bis(imino)carbazolide28 and

bis(cyclopentadienyl) manganese (Cp2Mn)6(a), tris(acetylacetonate) manganese

[Mn(acac)3],6(a) (salen)MnCl6(a) in combination with MAO, but no or only trace amounts

of polymer were isolated. In general, considerable lower activities are observed for

manganese complexes with ligands that provide very active catalysts with other late or

early transition metals. One report did introduce manganese catalyst with scorpionate

ligand that provided good activity for ethene polymerization when activated with

TIBA/[Ph3C][B(C6F5)4].29 In the study modified methylaluminoxane (MMAO) was also

employed as an activator resulting in lower activity. The produced polymers exhibit

moderate molar mass and unimodal narrow molar weight distribution. In addition, it was

proposed on the basis of results that coordinated anions (Cl-, Br- and NO3-) had influence

on polymerization reactions.

3.2.2 Polymerization Mechanism The conversion of the monomer into polymer depends on chain propagation and

termination rates, and therefore these rates determine molecular weight and molecular

weight distribution of the formed polymer. If the rate of propagation is slightly greater

than the rate of elimination, oligomeric products are formed. High molecular weight

polymers are produced when chain growth by insertion dominates the termination step. In

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this chapter mechanistical aspects of complexes bearing 2,6-bis(imino)pyridine ligands

catalyzed ethene polymerization are discussed.

The active species of α-diimine nickel and palladium catalysts is known to be a

cationic alkyl metal complex,4(b),30 but the nature of the active species of

bis(imino)pyridine complexes is still under investigation and discussion. In the case of

iron complexes, the active species is proposed to be a neutral31 or cationic4(b),24,32 alkyl

complex. Neutral cationic species are formed when, trialkylaluminums, including MAO,

bind Fe2+ centers, yielding neutral catalytically active species. Ethylene coordination

mechanism apparently involves releasing of a ligating group from iron to accept the

incoming monomer.10 Cationic monoalkyl Fe2+ species are supposed to form via methyl

abstraction from dialkyl complexes, but it has been shown with Mössbauer and electron

paramagnetic resonance (EPR) studies that Fe2+ centers of precatalysts are oxidized by

excess of MAO to Fe3+ species.33 The reduction Fe3+ species back to Fe2+ species by

MAO is also proved by 1H NMR and EPR studies.31(b) In addition, it is proposed that

different active metal centers may be the reason to the broad molar weight distribution

obtained with these catalysts.

Most studies report that the activation of Co2+ precursors involves the reduction of

Co2+ species to Co+ and their further transformation into cationic methyl derivatives with

MAO-based counterion.4(b),10 This assumption is based on the color change that

bis(imino)pyridine cobalt2+ complexes go through after addition of MAO excess. This

color change is similar to the color of bis(imino)pyridine cobalt+ alkyl complexes. These

alkyl complexes are reported to polymerize ethene after addition of MAO as dichloro

complexes. However, various ways for initiation are possible for bis(imino)pyridine

cobalt complexes.34

Although the initiating species is unknown the propagation is proposed to proceed

via Cossee-Arlman mechanism by sequential monomer coordination and insertion via a

transition state as presented in Scheme 2. Propagation continues until chain transfer takes

place. These chain transfer reactions include β-H transfer to metal (a), β-H transfer to

monomer (b) and chain transfer to monomer (c) (Scheme 3).10

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LMP

P

LM

LMP+ +

+

Scheme 2. Cossee-Arlman mechanism of chain propagation.

LMP

P

LMP

H

LMH

LM

P

R

AlR2

R2AlP

LMR

H

LM

P

LM

P

LM HP

P

LM

+

(a

(b)

(c

+

+

+

fast

slow

slow

fast

+

+

+ +

+ +

Scheme 3. Proposed chain transfer reactions in the polymerization of ethene with 2,6-

bis(imino)pyridine complexes of iron(II) and cobalt(II).10

3.3 Polymerization of Acrylates and Methacrylates

3.3.1 Radical Polymerization Acrylates are traditionally polymerized by free-radical methods.17 Radical species

for the initiation of polymerization can be formed for example by thermal decomposition

of such compound as benzoylperoxide or azobisisobutyronitrile (AIBN). Free radical

polymerization offers a little control over polymerization process and polymer properties.

To overcome the uncontrollability of the polymerization process, controlled radical

polymerization techniques have been developed. These include catalytic chain transfer

agent (CCT),35 stable free radical mediated polymerization (SFRP),36 reversible addition-

fragmentation chain transfer (RAFT)37 polymerization, and atom transfer radical

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polymerization (ATRP).38 The main idea in these techniques is to control the amount of

free radicals in order to ensure the consistent propagation. In ATRP and CCT metal

complexes are used to gain the control while in RAFT thio-compounds and in SFRP

nitroxides are utilized.39 CCT is generally used to synthesize macromonomers and the

polymerization is initiated with free radical initiators or haloesters and the technique uses

cobalt tetraporfyrines or glyoximes to remove a hydrogen atom from a growing chain end

and transfer it to the monomer to start new chains as shown in Scheme 4.35

CH3P

R

CH2P

RH

H CH2

CH3

RCH3

CH3

R

. + [Co(II)] [Co(III)]+

[Co(III)] + . + [Co(II)]

P = polymer chainR = esther group

Scheme 4. Mechanism for CCT of methacrylates.35

ATRP was reported independently by Matyjaszewski and Sawamoto in

1995.38(a),(b) The ATRP system needs a transition metal complex and an initiator with a

transferable halogen. Many types of halogenated compounds are potential initiators but in

general initiation needs to be faster than propagation and side reactions should be

minimized. The amount of the initiator determines the final molar mass of the polymer at

the full monomer conversion. A number of transition metal complexes have been applied

in ATRP. Complexes of late and middle transition metals are most efficient ones and

within those the copper complexes are the most extensively employed for the metal

catalyzed or controlled radical polymerization.38(a),40 Copper complexes bearing pyridine

and amine based ligands form the majority of complexes used in ATPR,38(a),(b) but some

iron based systems with nitrogen and phosphine ligands have been also efficiently

employed in ATRP.41 They are fascinating due to the low price and the non toxic nature

of iron. Also ruthenium, palladium, rhodium, rhenium, molybdenum, chromium and

nickel systems have been utilized as ATRP catalysts.38(a),(b)

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The polymerization mechanism for ATRP is based on transition metal catalyzed

reversible activation of carbon-halogen bond in a polymer chain by a transition metal

complex. Sawamoto has proposed a mechanism for ATRP and it is presented in Scheme

5.38(d) In well designed ATRP conditions chain growth is regulated and molar mass of a

polymer is increasing linearly as a function of time, which leads to narrow molar weight

distribution. Termination occurs via recombination of radical species or

disproportionation, but it is rather slow and in the ideal case polymerization ends when

all the monomer is consumed.

R X

CH2

R1

R2

R

R1

R2

H

H

CH2

R1

R2

R

R1

R2

X

H

H

R1

R2

PR

H

H

R1

R2

PR X

H

H

+ MnXnLm R. + Mn+1Xn+1Lm

. + Mn+1Xn+1LmMnXnLm

+

Mn+1Xn+1Lm+.

P = polymer chainR1 = H in acrylates and CH3 in methacrylatesR2 = esther grour

MnXnLm+

Scheme 5. Schematic presentation of ATRP by Sawamoto et al.38(b)

On the other hand, catalytic activity and selectivity is strongly ligand dependent in

ATRP.38(c) The ligand makes the transition metal salt soluble in the organic media and it

regulates the redox potential of the metal center for the appropriate reactivity and

dynamics for the atom transfer. The electronic and steric effects of the ligands are

important and the activity of N-based ligands in ATRP decreases with the number of

nitrogens coordinated to metal N4>N3>N2>>N1.38(b) Nitrogen ligands are most

commonly used and a wide variety of nitrogen ligands have been searched and utilized in

ATRP. The most common ones are a neutral chelating amine, imine or pyridine based

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ligands.38(b) A study by Sawamoto et al. showed that amine additives afford faster and

more controlled polymerization than corresponding phosphine compounds.42

The advantage in ATRP is a well defined polymer structure where the molecular

weight distribution is very narrow and the molar mass of polymer can be controlled by

regulating reaction conditions. By using multifunctional initiators, the polymer

architecture can be modified and star, branched or grafted polymers can be synthesized.

Polymer chains prepared by ATRP have halogen chain ends and thus they can be used as

macroinitiators for block copolymers. Practically, ATRP can be carried out either in bulk,

in solution, or in a heterogeneous system. The optimal temperature depends on the

monomer, the metal complex, and the desired molar mass, but typically elevated

temperatures are used. Though ATRP gives excellent control over polymer chain

structure, the major drawback in ATRP is the large amount of catalyst required leading to

residuals in the polymer.

3.3.2 Anionic Polymerization During the last decade the classical anionic polymerization of acrylates and

methacrylates has been modified towards more precisely controlled polymerization. The

main purpose has been to limit the undesired side reactions (Scheme 7). The mechanism

of anionic polymerization of acrylates and methacrylates can be described as Michael

reaction (Scheme 6). The apparent advantages of anionic polymerization of methacrylates

are the stereoselectivity of the reaction and the opportunities to modify the polymer

structures. Polymerization of acrylates with the method is more demanding because of

their higher reactivity towards nucleophiles and the presence of acidic hydrogen at the α-

position to the carbonyl group.43

R

OO

R*

IO

OR*

R

OO

R*

R

OO

R*

R

IO

OR*

RI- - -

R = H in acrylates and CH3 in methacrylatesR* = alkyl groupI- = initiator

Scheme 6. Initiation and propagation in anionic polymerization of acrylates and

methacrylates.44

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CH2

R

OOR*

CH2

R

OOI

R

OP

H

HOR*

CH2

R

OOR*

R

OP

H

HOR*

OCH2

R*

R

OP

H

HOR*

R

OOR*

PP

R

OP

H

HOR*

O

RPP

OO

P

R

RO

OR*

R

COOR*

R* OOR*

O

RCOOR*

R

R

P

I-M++ + CH3O-MR = H in acrylates and CH3 in methacrylatesR* = alkyl groupP = polymerchainM+ = counterionI- = initiator

- M+ + + CH3O-M

- M+ + + CH3O-M

-M+ CH3O-M+

A

B

C

D

Scheme 7. Side reactions in anionic polymerization of acrylates and methacrylates; A:

initiator destruction, B: monomer carbonyl attack, C: inter-molecular polymer

termination, and D: intra-molecular back biting termination.43 In all side reactions

produced methoxy anion (CH3O-) is too weak to initiate a new chain growth, thus

polymerization is slowed.

To avoid side reactions less nucleophilic initiator, polar solvent and low

temperatures are used in the polymerization process. Depending on the polarity of the

solvent and counter ion the stereostructure of the polymer can be tailored from isotactic

to syndiotactic in methacrylate polymerization. In polar solvent, propagating carbonium

ion and counterion can be described as free ions while in non polar solvent they form

tight ion pairs. For example, the polymerization of MMA in toluene with butyllithium at

–78 °C gives virtually 100% isotactic polymer and as the polarity is increased by addition

19

of polar additives, the counter ion is solvated and the degree of isotacticity is reduced

until in the absence of a nonpolar solvent quite high syndiotacticity is observed.45

Baskaran has stated that optimal condition for the anionic polymerization of

methacrylates is the use of bulky monofunctional initiator with bulky counterion in polar

solvent at low temperature.43

Besides classical anionic initiators, such as alkali metal alkyls (e.g. BuLi), a

variety of anionic polymerization initiators and methods have been studied to gain

controlled anionic polymerization. These methods use additives, mainly inorganic salts or

Lewis acids, to stabilize the propagating centers. Improvements have aimed to a better

control over polymerization as well as to the rising of the polymerization temperature to

the room temperature or above.43,46

The disadvantage of anionic polymerization is the cooling needed to suppress the

side reactions. In addition, anionic polymerization requires inert atmosphere, pure

reagents and clean glassware since all impurities lead to termination. These facts make

the method commercially uneconomic.

3.3.3 Group Transfer Polymerization Group transfer polymerization (GTP) was developed by Webster and Sogah at

DuPont, and it first appeared in the patent literature in the eighties.47 GTP is based on a

conjugated addition of silyl ketene acetals to α,β-unsaturated carbonyl compounds, such

as acrylates and methacrylates.48 The name originates from the proposal that the silyl

group transfers to new monomer during the monomer addition. However, Webster has

recently proposed that based on the existing evidence the original trimethylsilyl transfer

process is incorrect.46(a) Nevertheless, with GTP well defined polyacrylates and

poly(methyl methacrylates) can be prepared at room temperature and well above it.48(b)

Polymerization is accomplished most successfully in polar solvents.48(a) These are

advantages when compared to the living anionic polymerization that requires low

temperature and high purity reagents. Hence, GTP is currently used by DuPont to

produce dispersing agents for pigments and for emulsion stabilizers.46(a)

GTP uses 1-methoxy-1-(trimethylsiloxy)-2-methylprop-1-ene (MTS) as initiator

and nucleophilic anions or Lewis acids as catalyst. MTS is made by addition of

20

trimethylsilane to MMA. The most active nucleophilic catalysts are fluorides and

bifluorides while carboxylates and bicarboxylates operate better above ambient

temperature. Lewis acids, such as ZnCl2 and ZnBr2, are suitable catalysts, but they are

used within rather high concentrations.46(a) When nucleophilic anions are used as catalyst,

only a little amount of catalyst relative to the initiator is needed.

The function of a nucleophilic catalyst is to ease the displacement of the

trimethylsilyl group and the Lewis acidic catalyst increases the electrophilicity of the

double bond by coordinating to the carbonyl oxygen i.e. activate the monomers. The

degree of polymerization is governed by the ratio of monomer to initiator48(a) and it is

independent of the catalyst concentration which does affect the polymerization rate49.

The similarities between GTP and anionic polymerization are remarkable.50 Even

the characteristic back biting reaction (Scheme 7) has been found to be the main

termination reaction in GTP but the rates are much lower than for propagation. 51

No universal mechanism for GTP exists due to its dependence on the nature of the

catalyst and the exact reaction conditions but two types, associative and dissociative, can

be displayed (Scheme 8 and 9).46(a) Firm evidence for a dissociative anionic process at

room temperature and above was presented by Webster.46(a) On the other hand, the

mechanism of GTP differs with the type of catalyst used for the polymerization.43

OSiMe3

OMe

OSiMe3Nu

OMe

O

OMeMe3SiNu

MMA

O

OMe

PMMAMe3SiNuOSiMe3Nu

OMe

PMMA

OSiMe3

OMe

PMMA

+ Nu-

-

+

-

Nu-+

Scheme 8. The proposed mechanism for dissociative GTP pathway.46(a)

21

OSiMe3

OMe

OSiMe3Nu

OMe

O

OMe

MMA

OSiMe3Nu

PMMA OMeOSiMe3

OMe

PMMA

OSiMe3Nu

CO2Me

OMe

+ Nu- --

Nu-+ -

Scheme 9. The proposed associative mechanism.46(a)

In the dissociative mechanism (Scheme 8), nucleophilic catalyst (Nu-) complexes

with the silyl ketene acetal end groups and reversible forms an enolate that adds

monomer. Silyl ketene ends are reformed when enolate ends react with Me3SiNu. In the

associative pathway the nucleophilic catalyst is forming a complex with the silyl acetal

group. Subsequently the silyl group transfers to the incoming monomer and remains on

the polymer chain.46(a)

Here it is worth noting that a method similar to GTP based on methylaluminum

porphyrin for polymerization of acrylic monomers was developed by Inoue.52

3.3.4 Lanthanide and Early Transition Metal Complexes Yasuda and co-workers have reported organo rare earth metal complexes in the

polymerization of acrylates and methacrylates.53 They were able to isolate a

cyclopentadienyl samarium [Cp*2Sm(μ-H)]2 complex with two MMAs and determine the

crystal structure of adduct (Scheme 10 upper right corner) which supports a metal enolate

intermediate.53(e) In Scheme 10 the initiation mechanism based on the crystal structure is

presented.54 With this catalyst high molar mass polymer with narrow molar weight

distribution was obtained at -95 °C.

22

H CH2

OSm

O

CH2

O

Sm

O

OO

CH2

OSm

O

O

O

O

Sm

O

CH2

O

O

OO

MMA

MMA

Scheme 10. Polymerization of MMA according to Yasuda et al.54 Moreover, the polymerization of MMA with group 4 metals bearing Cp*2 ligands has

been reported.55 The polymerization was supposed to proceed via similar mechanism as

proposed to samarium complexes above.56

3.3.5 Late Transition Metal Complexes As in controlled radical polymerization (Chapter 3.3.1), late transition metal

complexes have been utilized in the polymerization of acrylates and methacrylates after

activation with MAO. There are reports describing complexes of nickel in the

polymerization of MMA.57 With nickel complexes the polymerization was suggested to

happen through monomer coordination to the metal center and subsequent insertion into

the nickel-carbon bond.57(b) The polymerization of methacrylates is also reported with

MAO activated iron,57(d), 58 cobalt,57(d) palladium59 and copper60 complexes. Palladium

diimine61 and β-diketiminato59(b) complexes are known to copolymerize ethene and

propene with acrylates. In general, these catalysts yield in branched polyethene in which

acrylate units are situated at the branch ends.

Furthermore, 2,6-bis(imino)pyridine iron(II)62 and cobalt(II)57(d) complexes and

phosphine complexes of iron26(b),62,63 and cobalt63 dichlorides were reported in the MAO

activated polymerization of tBA, MA and MMA. In the case of phosphine ligands, iron

23

catalysts were proven to be more active than their cobalt analogues and the activity, as

well as the molar mass of the produced polymer, was strongly ligand dependent.63

The polymerization mechanism for MAO activated bis(imino)pyridine iron(II)

complexes was studied by Castro.64 On the basis of ESI-MS and UV-Vis potential

initiation and polymerization mechanisms for the polymerization of tBA were stated. The

active species was proposed to be a cationic monomethyl complex and two potential

initiation pathways were suggested: iron-methyl bond homolysis and insertion of

monomer into the iron-methyl bond. The former case would lead into the radical

polymerization and the latter into the radical or coordination-insertion polymerization.

Based on end group analysis, i.e. the presence of ethyl saturated chain ends, termination

was supposed to occur via β-hydrogen transfer to the metal.

Nevertheless, distinguishing between radical, anionic, GTP and coordination-

insertion polymerization mechanism is difficult and no unequivocal mechanism for the

late transition metal mediated polymerization of acrylates and methacrylates can be

established.

3.4 Aluminum Complexes as Polymerization Catalysts There has been an interest in developing well-defined aluminum catalysts for

ethene polymerization,65 but there are only a few publications regarding definite

aluminum complexes as polymerization initiators for acrylates and methacrylates.

Aluminum alkyl catalysts would be a very interesting alternative to transition metal based

catalysts due to the low cost and simplicity of the ligands. Furthermore, these catalysts

would not require methylaluminoxane as cocatalyst. Hence, a catalyst based on

aluminum could be attractive and minor activity of aluminum catalyst compared to

transition metal catalysts can be approved. Ligand variation, a key to highly active

polymerization catalysts in transition metal chemistry, has emerged in the development of

aluminum catalysts for olefin polymerization. Ligands studied include those such as

bis(imino) pyridines,65(d) amidinates,65(a),(f) aminotroponiminates65(b) and β-

diiminates.65(c),(e) Although several groups have reported olefin polymerization with

aluminum alkyl complexes, the nature of active species remains non-specific. Moreover,

computational studies support only dimerization or oligomerization of olefins, but no

polymerization.65(h),66

24

Besides olefin polymerization, aluminium alkyl complexes could offer an

interesting alternative to the polymerization of polar monomers. Aluminum alkyls solely

are not capable conduct polymerization of acrylates and meth(acrylates)67 and they can

only be used in the purification of monomers for living anionic polymerization.68

Aluminoxanes have reported to polymerize MA63, MMA69 and tBAII though low molar

mass with broad molar weight distribution were observed indicating multi centre

behaviour.

Ikeda et al. described polymerization of acrylonitrile, MA and MMA with

aluminium alkyl complexes bearing mono- and bidentate Lewis base ligands such as

bipyridine and triphenylphosphine (PPh3).67(b)(c) They found that coordination of the

Lewis base to the central metal ion of the aluminum complex reduces the

electronegativity of the metal ion and increases the ionic character of the metal-carbon

bond which in turn induces the polymerization of polar vinyl compounds. In the nineties

Hatada et al. reported polymerization of MMA and other methacrylates with

triethylaluminum (TEA) and PPh3 or triethylphosphine (PEt3) in toluene at low

temperatures.70 The living polymerization yielded syndiotactic p(MMA) but bulky ester

group prevented syndiotactic propagation.

The polymerization of MMA with a combination of t-BuLi and aluminum alkyls

bearing bulky aryloxy substiuents (Scheme 11) at ambient temperatures and above was

reported by Ballard and co-workers.71 In their study it was found out that solvents, such

as tetrahydofuran (THF), inactivate the initiators by forming a stable complex with

aluminum alkyls.

O AlR

R = H, CH3

Scheme 11. Aluminum alkyls used with t-BuLi in the polymerization of MMA at room

temperature and above.71

The latest publications on organoaluminum complexes describe the

polymerization of tBA, MA and styrene. Okamoto et al. reported the polymerization of

25

tBA with TEA and PPh3, sparteine, (S)-BINAP, or n-BuLi at -78 °C but the study was

mainly concentrated on determining the relation between polymer tacticity and glass

transition temperature.67(d) In the study by Wu et al., bulky phenoxy aluminum

complexes, similar to aluminum alkyls described by Ballard,71 were active in initiating

the polymerization of MA and styrene at ambient and elevated temperatures.72 They

observed that electron withdrawing groups on the ligand enhanced the polymerization

activity. In the presence of catalytic amounts of radical scavengers, TEMPO and

Galvinoxyl, the polymerization of MA was inhibited, suggesting that radical species were

present in the polymerization reaction, but when the styrene was polymerized, radical

scavengers were not able to inhibit the reaction. The results made them conclude that

both radical and ionic species are involved in the polymerization depending on the

monomer used. On the other hand, it has been stated later that radical scavengers react

and deactivate metal based systems via coordination73 instead of inhibiting directly

radical reactions.74

3.5 Combinatiorial Approach in the Development of Polymerization Catalyst Combinatorial methods were originally developed for biochemical applications75

and drug discovery,76 but the methods can be applied to other fields of research as well.77

In the development of new polymerization catalyst, the traditional synthetic methods are

laborious and time-consuming tasks. High-throughput synthesis and screening

approaches to catalyst discovery and optimization and it is thoroughly changing the

techniques in which catalyst research is conducted.78 Increased rates of innovation, cost

effectiveness, reduced time and an improved probability of success are some of the

attractive features that are gained with combinatorial methods. The ability to assess large

number of ligands with sufficient steric and electronic diversity makes the method

fascinating for a rapid evaluation of various catalyst candidates of one specific metal for

polymerization reactions. After the best candidates are found, they can be fully

characterized, desired reaction conditions optimized and catalytic reactions further

studied.

Combinatorial chemistry includes both parallel synthesis and split and pool

methods. Parallel synthesis reactions are carried out in separate reaction vessels and each

26

product is analyzed with an appropriate method. In split and pool methods, various

reactants are mixed together in one reactor. If one of these set turns out to be active, then

subsequently, the combinations are screened individually and studied further. In practice

where a number of reactions are carried out at the same time can be classified under the

concept of combinatorial methods. The analysis methods and automation are in the most

important position when the possible numbers of simultaneous reactions are determined.

Manual methods reduce the amount of reactions to dozens while sophisticated automatic

methods enable hundreds of reactions and analysis in a short time.78(f)

The oxidation state and electronic configuration of the metal and the ligand

system in the catalytically active species are the key issues in the catalytic performance.

The catalytic properties of a certain metal complex generally are highly dependent on the

ligand framework around the metal center and by varying the ligand substituents, the

electronic character, geometry, and steric protection of the catalytic center can be

modified. There is no doubt that mechanistic understanding is valuable in the contouring

of a reaction course, but since the screening of a large number of potential catalysts

typically leads to a discovery of an active catalyst efficiently, the combinatorial method

has its benefits. Especially when a new type of catalysts is searched or new

polymerization reactions are studied combinatorial methods offer excellent tools by

speeding up the development process.

4 Results and Discussion

4.1 Experimental in General All solvents were dried with appropriate drying agents. Other reagents used in the

syntheses were purchased from commercial sources with high purity grade, and used as

such. Monomers in publication V were distilled over calcium hydride and stored under

argon in a freezer. All syntheses and polymerization experiments were performed under

argon atmosphere in a glove box or using standard Schlenk techniques. Detailed

descriptions of the solvent purification, ligand and complex syntheses, analyses, and

polymerization procedures and polymerization activities can be found in the experimental

parts of the attached original publications.

27

4.2 Synthesis and characterization of Manganese(II), Iron(II) and Cobalt(II) Complexes The condensation of amines with aldehydes or ketones in the presence of formic

acid catalyst is an easy way to synthesize imines (Scheme 12). The reaction can be

followed by IR spectroscopy since the strong aldehyde or ketone peak disappears and

new peaks appear due to the imine bond.

NR

O

R

O

MeOHHCOOH

R'-NH2 NR

N

R

NR' R'

+ 2

Scheme 12. Synthesis of 2,6-bis(imino)pyridine ligands.III

Tertiary imine ligands were synthesized from diamine and two equivivalents of

quinoline-2-carboxaldehyde in ethanol. Tertiary amine ligands were prepared from

secondary diamines and 2-bromomethylquinoline (Scheme 13). Isolated ligands were

identified by 1H NMR, 13C NMR, IR, mass spectroscopy, and elemental analysis.

NH2

NH2 NH

O

EtOH NN

NN

N

N

R

R

H

H NBr

N

N

R

R

N

N

EtOHK2CO3

+ 2

+ 2

R R

a: R =

b: R =

c: R =

d:R =

e: R =

Scheme 13. Preparation of tertiary amine and imine ligands.I,II,III

28

It should be mentioned that in the synthesis of N,N’-di(quinoline-2-methylene)-

1,2-phenylenediimine formation of two different products is possible as was observed in

this work.79,III As can be seen from the crystal structure (Figure 1); that instead of

diimine, a five member ring can be formed. Specific reason for that is unclear but proton

transfer is a competitive mechanism to the formation of imine leading to the formation of

the ring structure. The analyses of the ligand isomers revealed that 13C NMR spectra and

determination of the crystal structure are necessary since there is only a minor distinction

in 1H NMR spectra of these two compounds. In 1H NMR spectra the signals of two

protons of the five member ring species locate at δ = 6.30 (-N2-CH2-) and in the case of

imine ligand at δ = 8.80 (-N=CH-). While in 13C NMR 13 signals appeared for diimine

ligand and 17 for its ring species. Other analyses, i.e. MS and elemental analysis, yielded

similar results for these two forms. When this five member ring structure was allowed to

react with iron dichloride, a complex presented in Figure 1, was obtained.81 Though no

polymerization was carried out with this complex, it is interesting that iron is coordinated

with only to two nitrogen atoms of the ligand.

Figure 1. ORTEP drawing of the ligand with an unexpected structure and structure of

corresponding iron dichloro complex.80,81

All complexes prepared here (Schemes 14 and 15) are relatively stable and

straightforward to synthesize when compared to the very air and moisture sensitive early

29

transition metal complexes. The straightforward preparation of the complexes from the

corresponding ligand and metal salt in THF, CH2Cl2 or EtOH, was carried out at room

temperature. The complexes were characterized by IR, mass spectroscopy and elemental

analysis. In the IR spectra, imine complexes of iron and cobalt show a shift of υ(C=N)

stretching by ca. 30-60 cm-1 as compared to the free ligand. This reflects the coordination

of the imine nitrogen atoms to the metal. In the IR spectra manganese and tertiarty amine

complexes show only slight shifting. This indicates a weaker bond between the metal and

ligand and it is also seen in the elongated bond lengths of manganese complexes.IV It is

worth mentioning that manganese complexes (Scheme 14) active in polymerization were

found with combinatorial methods and this will be discussed later (Chapter 4.3). In the

procedure catalytic amounts of complexes were prepared in separate small glass reactors.

The ligand and metal salt were allowed to react together in THF and consecutively the

reaction solvent was replaced by toluene and used in the polymerization after activation

with MAO. The active manganese catalysts (Scheme14) were synthesized in a large scale

as described above.

N

N

N

N

MCl

Cl

N

N

N

N

MCl

Cl

N

N

N

N

MCl

Cl

N

N

R

R N

N

MCl

Cl

MnN

N

N

N

Cl

Cl

3: M = Fe4: M = Co5: M = Mn

1: M = Fe 2: M= Co

7: M = Fe, R = phenyl 8: M = Fe, R = benzyl9: M = Co, R = benzyl

6: M = Mn10

Scheme 14. Complexes bearing tertiary nitrogen ligands in this work.I,III,IV

30

MCl Cl

NR

N N

R

R' R'

11: M = Fe, R = CH3, R' =

12: M = Fe, R = H, R' =

13: M = Fe, R = CH3, R' =

14: M = Fe, R = CH3, R' =

15: M = Co, R = CH3, R' =

16: M = Fe, R = CH3, R' =

17: M = Fe, R = H, R' =

18: M = Co, R = H, R' =

19: M = Fe, R = CH3, R' =

20: M = Fe, R = H, R' =

21: M = Co, R = H, R' =

22: M = Fe, R = H, R' =

23: M = Co, R = H, R' =

Scheme 15. Complexes bearing tridentate nitrogen ligands. II,III,81

The single crystal X-ray structure of the cobalt complex 23 (Figure 2.) and

manganese complexes 5, 6 (Figure 3) were determined. Suitable crystals were obtained

by slow evaporation of the solvent. The coordination of Co(II) can be described roughly

as a distorted trigonal bipyramide in 23, while distorted octahedral coordination is

observed in Mn complexes.

In complex 23, imino nitrogen atoms occupy the axial positions and chlorines and

a nitrogen atom at pyridine form the trigonal plane. The imino nitrogens are shifted to the

opposite sides of the plane formed by the pyridine and cobalt, while bornyl-sybstituents

are positioning above and below the N3Co plane. Bornyl-substituents were unable to

displace CoCl2 from the N3Co plane to the square pyramidal arrangement as happened

with earlier reported cobalt(II) complex bearing 2,6-diacetylpyridinebis(2,6-

diisopropylanil) ligand.24

31

Figure 2. Solid state structure of cobalt complex 23.II H-atoms, the second cobalt

complex and CHCl3 solvent molecules were omitted for clarity.

In complexes 5 and 6 the chiral bridging twists the N4-Mn basal plane and thus

causes a substantial rhombic distortion in octahedral geometry of Mn(II). Twisting bends

chlorine atoms from the apical position towards the cis-configuration. In complex 5, for

the two independent molecules at the unit cell, the Cl-Mn-Cl angles were 132° and 135°

and the distorted N4-Mn basal planes were practically perpendicular to the plane of

MnCl2. In 6 the pyridine nitrogen atoms are shifted away from the N4-Mn basal plane and

planes defined by N1-Mn-N2 and N3-Mn-N4 are bisecting each others with an angle of

49.0(2)º. The N2-Mn-N3 plane is perpendicular to the plane of MnCl2.

The NPy-Mn bonding with the bis(imino)pyridine ligand is remarkably shorter

(2.20 Å)82 than quinoline N-Mn bonding in 5 (2.49-2.51 Å) and 6 (2.32 -2.34 Å). This

noticeable difference in the coordination strength of the pyridyl lone pairs, together with

the elongated Mn-Cl bonds, might have significance when it comes to catalytic properties

of these Mn-complexes. Similar elongation of the N-Mn bond lengths, as in 5 and 6, can

be found, although to a lesser extent, from the previously published solid state structures

of [di(pyridine-2-methylene)diiminocyclohexane]MnCl283 and bis(bipyridine)MnCl2.84

Furthermore, the elongated NPy-Mn bonds lead to reduced electron donation from the

ligand and increase Lewis acidity of Mn. This might explain the observed ethene

polymerization activity of 5 and 6 after MAO activation.

32

Figure 3. Crystal structures of manganese(II) complexes 5 and 6.IV H-atoms and CH2Cl2

solvent molecules were omitted for clarity as well as the second manganese complex in

asymmetric unit of 5.

In order to activate transition metal complexes for olefin polymerization, they are

often converted to corresponding alkyl derivatives by the treatment with aluminum

alkyls, most commonly in situ with MAO. Such alkyl complexes are considered as

prerequisite for the formation of metal alkyl cations, generally considered as catalytic

active centers for olefin polymerization. Thus transition metal alkyl complexes,85

including manganese alkyl complexes, 86 are of significant interest.

Hence, complexes 5 and 6 were allowed to react with benzyl magnesium chloride

(BzMgCl) in diethyl ether (Et2O). Both complexes gave only monosubstituted alkyl

complexes (Scheme 16). Later attempts to introduce a second benzyl group by treatment

with excess of BzMgCl were unsuccessful and only monosubstituted species were

isolated. Both of the monobenzyl substituted complexes were adequately stable allowing

the characterization by EI-MS, HR ESI-MS and IR.IV

The methylation of complexes 5 and 6 with methyl magnesium bromide

(MeMgBr) yielded extremely air and moisture sensitive products, which were identified

by HR ESI-MS methods as alkyl derivatives. Due to air sensitivity and rapid

decomposition IR and EI-MS gave inaccurate results in analyses.IV

33

N

N

N

N

MnCl

Cl

N

N

N

N

MnCl

Cl

MgBr N

N

N

N

MnCl

MgBr N

N

N

N

MnCl

MgBr

MgBr

LMnMe2

LMnMe2

5

6

Scheme 16. Preparation of manganese alkyl complexes.IV Reaction conditions: -78 °C in

Et2O in an argon glovebox.

4.3 MAO Activated Manganese(II) Complexes in the Polymerization of Ethene Due to the rarity of manganese complexes in the ethene polymerization, the

combinatorial approach was chosen as a method to study manganese complexes in MAO

activated ethene polymerization. Since MAO and MMAO are the most active and used

co-catalysts in late transition metal mediated ethene polymerization,10 MAO was

employed.

In separate reactors in situ prepared complexes were activated with MAO.

Subsequently, the activated complexes were sealed in a 1 L steel reactor and the reactor

was charged with ethene pressure. In the primary screening three active manganese

catalysts (5, 6 and 10 in Scheme 14) were found and these complexes were then

synthesized as described in the previous chapter.

When the ethene polymerizations were carried out separately in large scale, a

rather sensitive activation of the complexes was observed. If the complexes were first

treated at room temperature with MAO and then heated to the desired polymerization

temperature, reproducible activity levels were achieved. By contrast, catalysts exhibited

34

no or very poor ethene polymerization activities when MAO treatment was done at

elevated temperatures.

The highest activity [67 kgPE/(molcat x h)] among these manganese catalysts was

reached with the MAO activated complex 5 at 80 °C and under 5 bar of ethene pressure.

Polymers produced at 60 °C exhibited very high molar masses (1200-1700 kg/mol) with

relative narrow molar weight distribution, though slight tailing towards the low molar

mass region was observed. The rise in the polymerization temperature from 60 °C to 80

°C led to PE with clear bimodal molar weight distribution and a decrease in molar mass.

Despite of variations in polymerization conditions, activity of the biphenyl-bridged 6 and

the unbridged complex 10 remained low. Both of them produced high molar mass

polyethene with bimodal molar weight distribution.

The bimodality of the polymer strongly suggests the presence of two different,

structurally defined catalytic active centers. Probably, high polymerization temperature

causes intramolecular fluctuation of the coordination sphere of the activated manganese

complexes. The existence of structural isomerization of similar manganese complexes

has been verified by crystal structure determination,87 and the three possible

conformational isomers for tetradentate ligands in an octahedral coordination sphere have

been illustrated.88 In addition, similar fluctuation of the complex geometry during the

activation has been reported for Fe(II) derivatives of 6 by Brintzinger et al.89

Alkyl complexes presented in Scheme 16 were also studied in ethene

polymerization. Complexes were activated with TIBA/B(C6F5)3, but the activated alkyl

complexes were extremely unstable and their transfer into the polymerization reactor

without a minor air contact was very complicated. In general, MAO activated dichloro

complexes were more active than corresponding TIBA/B(C6F5)3 activated alkyl

complexes. The instability of the activated alkyl complexes might induce the poor

polymerization behavior.

To conclude, with combinatorial methods new active manganese catalysts for

ethene polymerization were found and three essential requirements for the active

manganese(II) catalyst precursors can be summarized: 1) they are six-coordinated, 17-

electron species 2) there is the presence of ligands with imine pyridine/quinoline moieties

separated by two carbon atoms and 3) distortion of octahedral configuration of the

manganese by the ligand framework.IV

35

4.4 Manganese(II), Iron(II) and Cobalt(II) Complexes in the Polymerization of Acrylates

4.4.1 Tert-butyl Acrylate It became apparent from this study that there are several factors affecting the

polymerization as well as the properties of the polymers. Firstly, the ligand’s structure

and the metal are the significant factors determining the polymerization behavior.

However, the reaction conditions, e.g. monomer concentration, temperature and reaction

time, have major influences on polymerization activity and material properties within

these complexes.

As can be seen in Figure 4, the metal has an essential effect on the monomer

conversion and molar mass. Iron complexes are more active than their cobalt analogues

and produce also polymers with remarkable higher molar mass. Similar results have been

observed in ethene polymerization with complexes of 2,6-bis(imino)pyridine

ligands.24,25(b) It is reasonable to assume that the different configuration of d-electrons or

activation processes90 of cobalt complexes are accountable for the observed phenomenon.

Manganese complex 5 is the least active (Figure 5) within the complexes bearing the

same ligand structure, but it produces relative high molar mass (Figure 6).

020406080

100120140160180

20 21 22 23Complex

Mw (k

g m

ol-1

)

FeCo

0

10

20

30

40

50

60

70

80

20 21 22 23

Complex

Con

vers

ion

(%)

FeCo

Figure 4. Comparison between iron and cobalt complexes bearing tridentate nitrogen

ligands in the polymerization of tBA.

The influence of the ligand’s structure on polymerization is diverse. However,

this versatility brings possibilities that affect the polymerization and produced materials.

Within the complexes bearing tridentate nitrogen ligands, aldimine-derivated ones are

36

more active than their ketimine analogues (Figure 5 complex 12 vs. 11 and 20 vs. 19).

This is contrary for reported to ethene polymerization activity with catalysts of this

type.22(b),23(b),24 No conclusion can be drawn regarding which structure is better on the

basis of molar masses, because aldimine complex 12 produces higher molar mass than its

ketimine analogue 11 while aldimine complex 20 produces lower molar mass than the

corresponding ketimine complex 19.

Substituents on the imino nitrogen atoms have only a minor effect on the

polymerization activity within ketimine complexes of iron, namely complexes 11, 13, 16

and 19 (Figure 5). However, complexes bearing aliphatic substituents, i.e. 13 and 19,

produced polymers with a higher molar mass than complexes 11 and 19 with aromatic

groups (Figure 6). A similar effect is not observed within aldimine complexes 12, 20 and

22. Within these three complexes, 12 with aromatic substituents on the imino nitrogen, is

the most active and produces polymer with the highest molar mass.

0

10

20

30

40

50

60

70

80

90

100

1 2 3 4 5 7 8 9 11 12 13 16 19 20 22

Complex

Con

vers

ion

(%)

Fe

Co

Mn

Figure 5. Selected examples of monomer conversion in the polymerization of tBA.III,81

Polymerization conditions: [tBA] = 3.0 M, ncat = 2.0 μmol, MAO:M = 250, RT,

tpolymerization = 24 h, solvent toluene.

37

0

50

100

150

200

250

300

350

400

450

1 2 3 4 5 7 8 9 11 12 13 16 19 20 22

Complex

Mn

(kg

mol

-1)

Fe

Co

Mn

Figure 6. Selected molar masses of p(tBA). Polymerization conditions as above in Figure

5.

For a more detailed study on the effect of the ligand and metal on tBA

polymerization activity, four complexes bearing tri- and tetradentate nitrogen ligands,

namely 3, 4, 14 and 15, were chosen. In addition, MAO only and MAO activated iron(II)

chloride was included in the study. Gas chromatography (GC) methods were utilized in

determination of monomer conversion. Samples from the polymerization vessel were

taken sequentially during the first two hours of the polymerization. Figure 7 shows that

polymerization proceeds very fast in the beginning but after a certain polymerization

time, the differences in initial activities e.g. within iron complexes are equalized.

38

0 20 40 60 80 100 120 1400

200

400

600

800

1000

1200 14: Mn= 103 kg/mol

15: Mn= 68 kg/mol

3: Mn= 103 kg/mol

4: Mn= 19 kg/mol

FeCl2: Mn= 127 kg/mol

cocatalyst MAO

Activ

ity (k

g po

lym

er/(m

olh)

)

Time (min)

Figure 7. Polymerization activity in the polymerization of tBA was elucidated by GC

methods. Conditions n(cat) = 2 µmol, [tBA] = 1.1 mol/l, MAO:complex = 250:1, in

toluene at room temperature.III

In the beginning of polymerization, complexes 14 and 15 bearing tridentate

nitrogen ligand, yielded higher activity than complexes 3 and 4 with tetradentate ligands.

This can be related to their structure; in a solid state, iron(II) complexes with tetradentate

ligands, prefer octahedral coordination sphere,88,91 while structural fluctuation between a

square pyramidal and a trigonal bipyramidal geometry has been reported for the tridentate

complexes.24 In addition, five coordination and cis orientated chlorines in tridentate

complexes are advantages in polymerization.

Furthermore, polymerization conditions have significant effects on the

polymerization activity and produced material properties. As seen above, polymerization

time not only has a strong effect on activity, but it also has an influence on molar masses.

In the study with iron and cobalt complexes bearing tetradentate nitrogen ligands the

produced molar masses doubled when the polymerization time was increased from 12

hours to 24 hours.81

39

Increase of monomer concentration increased the conversion, polymerization

activity and molar mass of the produced polymers as can be seen in Figures 8 and 9. The

linear enhancement in molar masses with the increasing monomer concentration occurred

with all studied complexes. With the highest monomer concentration 6.4 M (bulk) the

highest molar masses obtained were 1900 kg/mol while with low monomer concentration

(0.6 M) molar masses as low as 5 kg/mol were obtained.III,81

Figure 8. Selected conversions of tBA polymerization in different monomer

concentrations. Polymerization conditions: ncat = 2.0 μmol, MAO:M = 250, RT,

tpolymerization = 24 h, solvent toluene.III,81

30

40

50

60

70

80

90

100

110

0 1 2 3 4 5 6 6.5 [tBA]

3 4 11 12

Con

vers

ion

(%)

40

Figure 9. Selected molar masses of tBA-polymers in different monomer concentrations.

Polymerization conditions: ncat = 2.0 μmol, MAO:M = 250, RT, tpolymerization = 24 h,

solvent toluene.III,81

The influence of temperature has been studied with 2,6-bis(imino)pyridine

iron(II) complexes26(b) in tBA polymerization and phosphine complexes of iron(II) and

cobalt(II)63 in MA polymerization. The results on polymerization activity with iron(II)

and cobalt(II) complexes bearing tetradentate nitrogen ligands concurred with those

results and activity was increased as polymerization temperature increased.III However, a

more interesting issue is the relationship between temperature and molar mass. As the

temperature was increased from 20 °C to 70 °C, the molar mass was decreased in the

series of 2,6-bis(imino)pyridine iron(II) complexes,26(b) while the molar mass was

increased up to 40 °C within the complex group bearing tertiary nitrogen ligands.III Until

some point between 40 °C and 60 °C molar masses started to decrease. Similar behavior

was observed for phosphine complexes of iron(II) and cobalt(II).63 The possibility of

ligand dissociation from the complex was overruled by the polymerization experiments

on MAO activated metal salts.63 Thus, the decrease in molar mass originates from an

increased chain termination rate. In addition, variation in polymerization temperature had

no significant influence on the polymer microstructure when the polymerizations were

0

200

400

600

800

1000

1200

1400

1600

1800

0 1 2 3 4 5 [tBA]

3 4 11 12

Mn(

kg m

ol-1

)

41

carried out above 0 °C,III,63 but lowering the temperature to -78 °C increased the [rr]

triads.III

In earlier polymerization studies of MMA with NiCp*2 and Ni(acac)2 complexes

it was observed that large amounts of MAO are not required.92 It was found that the

optimal Ni:MAO ratio was 1:100. On the other hand, the influence of the Fe:MAO ratio

has been studied in detail with iron(II) phosphine complexes.63 There, maximum activity

was reached at a ratio of 1:125 and 1:250 after which the activity lowered and remained

at constant level. The molar mass decreased sharply until a constant level at the ratio of

1:500 is settled. With iron(II) and cobalt(II) complexes bearing a tetradentate nitrogen

ligand, similar dependence on MAO amount was observed.81

It can be concluded that in the polymerization of tBA the activity and molar

masses of polymers are influenced by the ligand structure and the choice of metal centre

and with different polymerization conditions various polymer materials were produced.

However, based on the results no mechanism for transition metal assisted

polymerizations can be conducted.

4.4.2 Other Acrylates and Methacrylates The polymerizations of methyl acrylate and methyl methacrylate were also carried

out with iron(II), cobalt(II) and manganese(II) complexes bearing tetradentate nitrogen

ligands.I,III,IV Polymerization of MMA was carried out under ATRP conditions with in

situ prepared iron dichloro complexes from ligands a-d (Scheme 13).I The

polymerizations were activated with ethyl-2-bromoisobutyrate. It was observed that the

steric effect of ligand determine the solubility of the catalyst as well as the selectivity.

The polymerization activity of the in situ formed iron dichloro complexes was in the

order of: a > c > b, while iron dichloro complex of ligand d was inactive.

The polymerization of MMA was also accomplished with MAO activated

complexes 1, 2 and 3 (dichloro complex of ligand d).III However, conversions and molar

masses remained low. Furthermore, these complexes were employed in the

polymerization of MA resulting in slightly better conversion and moderately higher

molar masses than in the polymerization of MMA. With both monomers, iron complex 3

42

gave the highest molar masses and cobalt complex 2 the lowest ones. A similar effect is

seen in the polymerization of tBA.

MAO activated manganese complex 5 was more extensively employed in the

polymerization of various acrylates and methacrylates (Table 1).93 It was observed that

acrylates were polymerized easier than methacrylates. The molar mass of the produced

polyacrylates is found to increase as the size of the ester group increased. With

methacrylates, rather low conversions were obtained though poly(ethyl methacrylate)

exhibited a substantially high molar mass. Furthermore, the molar mass of poly(methyl

methacrylates) produced with 5 (36 kg/mol) is greater than molar mass obtained with the

corresponding iron complex 3 (4.3 kg/mol). In the polymerization of tBA it was also

noticed that manganese complex 5 was able to produce a rather high molar mass though

conversion remained low (Chapter 4.4.1).

Table 1. Polymerization of acrylates and methacrylates with MAO activated 5.

Polymerization conditions: solvent toluene, RT, c(monomer) = 3.0 M, n (cat) = 2.0 µmol,

[Al]:[Mn] = 250, polymerization time 15 hours.93

Monomer Mnx10-3 Mw/Mn Activity Tg

c(ºC) Methyl acrylate 79 2.47 20.4 21

Ethyl acrylate 133 1.64 20.8 -15

Butyl acrylate 206 1.60 36.0 -

Tert-butyl acrylate 316 1.83 14.8 48

Methyl methacrylate 36 1.78 3.3 91

Ethyl methacrylate 225 1.55 8.8 -

4.5 Parallel screening of Aluminum Complexes Combinatorial screening was chosen as a method to find new aluminum based

catalysts since very scarce studies have been carried out with aluminum alkyl complexes

in the polymerization of acrylates and methacrylates. The set up for the screenings was

very simple and aluminum complexes for the polymerization were formed in situ by

stirring a ligand with aluminum alkyl in toluene. Consecutively, a sufficient amount of

43

monomer was added to the reaction vessels through septa. Polymerization reaction

conditions for the primary screening (temperature, monomer to initiator ratio, solvent)

were chosen on the basis of our earlier studies with acrylates.III,26(b),62,63,81

4.6 Aluminum Complexes in the Polymerization of Acrylates and

Methacrylates

4.6.1 Tert-butyl Acrylate Aluminum alkyl complexes form an interesting group of compounds for the

polymerization of acrylates and methacrylates assuming that no co-catalyst are required

with them. For the primary screening, 19 ligands (Scheme 17), including phosphines,

salicylaldimines and nitrogen ligands, were selected. The ligands for the primary

screening were selected on the basis that their transition metal complexes were already

known to be active in polymerization reactions.III,4(b),10,22,26(b),62,63 ,94

44

Scheme 17. Ligands employed in the primary screening of aluminum complexes.V

In the primary screening 57 aluminum alkyl complexes were employed in the

polymerization of tBA. In Figure 10 it can be seen that with a couple of exceptions all

complexes were able to initiate the polymerization of tBA to some extent. However, the

major finding from the primary screening was that all phosphine ligands with triethyl

aluminum (TEA) or triisopropyl aluminum (TIBA) as aluminum alkyl led to the

quantitative polymerization of tBA. Additionally these polymerizations afforded high

molar masses (from 50 to 150 kg/mol) with relatively narrow molar weight distributions

(MWD ~2). Hence, various phosphines were selected for the further studies.

NOH

F

FF

FF

NOHNOHNOH

FNOH

NOH

OMeOMe

OMe

NN N NH

F

F F

F

N N

N NH

iPr iPr

iPr

OH

N

OH

N OH

N

OH

N

OH

N

OH

N

N

N

N

NN

N NP P P

NMe2 PPh2

N N

1 2 3 4

6

5

9 107

1311

16

1514

17

iPr

18

12

8

19

45

Figure 10. Monomer converision in the primary screening of aluminum complexes.V The

reaction conditions used were room temperature, [tBA] = 1.1 M, n(complex) = 150 μmol,

monomer to initiator ratio (M:I) = 47, solvent toluene. The ligands that correspond to the

ligand numbers are shown in Scheme 17.

Scheme 18. Phosphine ligands used in the second screening.V

P P P P

PP 3

P 3

P 3

P 3

P 3

P 3

PCl

Cl Cl

P 3

PPh

Ph

P

F F

F

FF3

11

2 3

7 8 109

4 5 6

13 14 12

1

15

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 TIBA

TEA

TMA

0

20

40

60

80

100

Con

vers

ion

%

Ligand

TIBATEATMA

46

In Scheme 18, the phosphine ligands for the second screening are presented. The

selection criteria were different bulkiness and donor-acceptor properties as well as

commercial availability and affordability. Furthermore, the steric and electronic

properties of phosphines are easily modified,95 and typically a direct relation between

catalyst performance and the properties of the phosphine ligand could be established.96

Result from the secondary screening showed that, besides the phosphine ligand,

aluminum alkyl has a remarkable effect on the polymerization activity. In general,

trimethyl aluminum (TMA) yielded lower conversions than the other aluminum alkyls

(Figure 11). However, ligands 4, 10, 11, 12 and 13 (in Scheme 18) with TMA were able

to produce a high molar mass poly(tBA).

Figure 11. Monomer conversions in the secondary screening.V Polymerization conditions

as in the primary screening. The ligands that correspond to the ligand numbers on the

horizontal axis are shown in Scheme 18. Polymerization conditions as in Figure 10.

In general, phosphines with phenyl moieties (e.g. 11 and 12) formed the most

active combinations and produced the highest molar masses. While phosphines with alkyl

substituents (e.g. 2) or electron withdrawing groups (e.g. 1 and 14) yielded low

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15

TMA

TEA

TIBA0

20

40

60

80

100

Con

vers

ion

%

TMATEATIBA

47

polymerization conversions and relatively low molar masses. Increasing the steric bulk in

the phenyl ring (e.g. 13 and 15) had a similar effect.

The effect of solvent, reaction temperature and monomer concentration were

studied with triphenyl phosphine (PPh3) (8) and aluminum alkyls.V Polymerization was

carried out in tertahydrofuran (THF), acetonitrile (AcN), ethyl acetate (EtOAc) and

toluene (the solvent in the primary screening). When compared to the polymerization in

toluene THF was the only solvent where the conversion was diminished. However, the

molar masses of the produced polymers in THF, AcN and EtOAc were lower than those

made in toluene with TEA and TIBA as aluminum alkyls. When TMA was used, high

conversions were reached in EtOAc and AcN. In EtOAc, a substantially high molar mass

was observed. Thus, the polymerization can be carried out in various solvents.

Here, the similar enhancement in molar masses of produced polymers with

increasing monomer concentration was observed as in the polymerization of tBA with

iron and cobalt complexes.III When the reaction temperature is elevated, molar masses are

decreased and molar weight distribution broadened, probably due to the increased chain

transfer reactions. Decreased polymerization activity at high temperatures indicates that

the aluminum species are thermally labile. At temperature under ambient molar mass

increases and molar weight distribution approaches value 1, which is indicating living

polymerization.

Figure 12 shows the comparison of produced molar masses of p(tBA) between

iron(II) and cobalt(II) complexes bearing tri- and tetradentate nitrogen ligand and

aluminum alkyl complexes. It should be mentioned that catalyst loading was greater in

the polymerizations with aluminum alkyl complexes. Due to the different catalyst

amounts, a general conclusion on behalf of either complex group can not be drawn.

Nevertheless, molar masses produced with these complexes diverge and phosphine

ligands 11 and 12 with TMA and TEA, ligand 10 with TMA, and 8 with TEA are

producing higher molar masses than the other complexes.

48

0

50

100

150

200

250

comple

x 3

comple

x 4

comple

x 14

comple

x 15

8/TMA

8/TEA

8/TIB

A

10/TMA

10/TEA

10/TIBA

11/TMA

11/TEA

11/TIBA

12/TMA

12/TEA

12/TIBA

Mn (

kgm

ol-1

)

Figure 12. Comparison between molar masses of poly(tBA) produced with selected iron

and cobalt complexes bearing tri- and tetradentate nitrogen ligandsIII and aluminum alkyl

complexes bearing phosphine ligandsV.

4.6.2 Methyl Methacrylate Subsequently, the most active phosphine ligands, i.e. 5-12, from tBA

polymerization and TIBA as aluminum alkyl, were employed in the polymerization of

MMA to gain differences between these complexes. With ligand 10 little conversions

with low molar masses were observed while conversions 60 % and over were yielded

with other combinations. Increasing monomer concentration clearly enhanced the

conversion with TIBA complexes of ligands 5 and 7, but the effect can not be seen with

other studied combinations because of the almost complete conversions obtained. Figure

13 shows that the molar masses of produced pMMAs are growing as the monomer

concentration is increased. The highest molar masses are produced with PPh3 (8), tri(m-

tolyl) phosphine (11) and tri(p-tolyl) phosphine (12). These all yielded conversions over

80 % with rather narrow molar weight distribution (under 2).

49

5 6 7 8 9 10 11 12

100

200

4000

50

100

150

200

250

300

Mn [

kg m

ol-1

]

Ligand

M:I

Figure 13. Molar masses of poly(MMA) with PPh3TIBA.V The reaction conditions: RT,

n(complex) = 150 μmol, monomer to initiator ratio (M:I) 100, 200 and 400, in toluene.

The ligands that correspond to the ligand numbers are shown in Scheme 18.

4.6.3 Proposed Mechanism for Polymerization of MMA First, to ensure the complex formation in the screening PPh3 and TEA or TIBA

were allowed to react and subsequently the formed complexes were studied in detail.

The complex of PPh3 and TEA crystallized as colorless crystals. In the complex (Figure

14) PPh3 is bound to TEA and the phenyl rings of the ligand are in a propeller shape

conformation and aluminum adopts a distorted tetrahedral geometry. Furthermore, both

complexes were identified by 1H NMR, 13C NMR, and ESI-MS.97

50

Figure 14. An ORTEP drawing of (PPh3)TEA.V Thermal ellipsoids were drawn on a 30

% probability. H-atoms and C6b atom in the disordered ethyl group (C5-C6) were

omitted for clarity.

For the mechanism studies, PPh3TIBA complex was employed. In ESI-MS, MS-

MS and NMR studies, it was confirmed that the coordination of MMA is taking place via

a carbonyl oxygen to PPh3TIBA complex (Scheme 19 left). In addition, enolization of

MMA was observed (Scheme 19).V The resonance structures of MMA·AlR3 adducts and

NMR shifts for phenolate complexes have been studied earlier,98 therefore an analogous

monomer activation is taking place. The coordination via carbonyl was also demonstrated

with methyl isobutyrate (MeiB). The shifts in NMR signals were analogous to those of

MMA except for the double bond that is absent in the MeiB, thus enolization is

impossible with MeiB. A possible pathway for the propagation is via 1,4-conjugated

(Michael) addition (Scheme 20) as proposed for GTP, but the precise mode of

propagation remains open. No evidence for an associative or dissociative pathway nor a

monometallic or bimetallic system can be provided. Furthermore, the ability for part of

the aluminum complex to act as monomer activator or propagator can not be excluded.

The role of phosphine ligands in the polymerization is to accept and donate

electron density during the polymerization process and facilitate the propagation step.

The phosphine ligand remains coordinated to aluminum throughout the process as no

changes in 13C-NMR signals of the phenyl group in PPh3 were observed during the

51

polymerization. Further, phosphine end groups were absent in NMR of polymers, though

PPh3 residues were observed.

P

AlR

R

R

P

AlR

R

RO

O

O

O

O

O

P

Al

R

R

R

R = isobutyl, C4H9 Scheme 19. The addition of first monomer (MMA) to the PPh3Al(C4H9)3 complex.

O

O

P

AlRR

R

O

OOO

O

OR

P

AlRR

OO

O

Opolymer chain

P

AlRR

R = isobutyl, C4H9

MMAMMA

Scheme 20. Representation of the proposed polymerization mechanism via a series of

conjugated additions.

52

5 Conclusion In this thesis, versatile complexes of manganese, iron, cobalt and aluminum were

synthesized and employed in the polymerization of acrylates and methacrylates. High

polymerization activity was gained and varying polymer properties were produced

depending on the complex structure and reaction conditions. The choice of catalyst and

the tuning of the polymerization conditions, enabled control of the polymer structure

from a low to high molar mass product with narrow molar weight distributions.

All preparations of ligands and complexes were straightforward to carry out. After

activation with MAO iron, cobalt and manganese complexes were efficient in the

polymerization of tBA and iron complexes with tridentate 2,6-bis(imino)pyridine ligands

turned out to be the most active ones. Moreover, the polymerization of other acrylates

and methacrylates were demonstrated with these MAO activated complexes.

Furthermore, this work confirmed the efficiency of combinatorial methods in

finding new active complexes for the polymerization reactions. Parallel screening

allowed a wide variety of ligand and metal combinations to be studied in a short time and

resulted in the discovery of new polymerization catalysts for ethene, acrylates and

methacrylates. Particularly, a series of aluminum phosphine complexes which were able

to polymerize tBA and MMA to total conversion are interesting new catalysts.

The polymerization mechanism of MMA is suggested to begin with the first

monomer coordination via a carbonyl group to aluminum alkyl complex, followed by

enolization of the monomer. Propagation is proposed to take place via 1,4-conjugated

addition as presented for GTP (Chapter 3.3.3). However, the intimate propagation mode,

i.e. monometallic vs. bimetallic and associative vs. dissociative, remains open. As the

reaction mechanism of the transition metal assisted polymerization of acrylates and

methacrylates is ambiguous, each stated mechanism interpretation will hopefully carry

the research further.

53

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