Transcript

Organometallic Organometallic CatalystsCatalysts

Presenter : Saber Askari

Advisor :

Dr.Mirzaaghayan

May 2012

Contents :Contents : The basis for catalysisThe basis for catalysis

Catalytic Cycle

History

Mechanistic Concept

Homogeneous CatalysisHomogeneous Catalysis

Wilkinson’s Catalyst

Asymmetric hydrogenation

Hydroformylation

Monsanto Acetic acid Process

CATIVA Process Wacker Process

Heterogeneous CatalysisHeterogeneous Catalysis

Ziegler-Natta Catalyst

A Catalyst is a substance which speed up the rate of a reaction without itself being consumed.

A catalyst lowers the activation energy for a chemical reactionThe catalyzed reaction goes by a multistep mechanism in which the metal stabilizes intermediates that are stable only when bound to metal .

The basis for catalysis

Importance of catalysis

Many major industrial chemicals are prepared with the aid of catalysts Many fine chemicals are also made with the aid of catalysts– Reduce cost of production– Lead to better selectivity and less waste

Catalytic Cycle

The catalytically active species must have a vacant coordination site to allow the substrate to coordinate

Late transition metals are privileged catalysts (from 16e species easily)

In general , the total electron count alternates between 16 and 18One of the catalytic steps in the cycle is rate-determining

The establishment of a reaction mechanism is always a difficult task. It is even harder to definitively establish a catalytic cycle as all the reactions are going on in parallel!

History

Fundamental Reaction

Mechanistic Concept

Homogeneous CatalysisHomogeneous Catalysis

Wilkinson`s Catalyst : Olefin HydrogenationHydroformylation

Monsanto Acetic acid Process

Wacker Process

Heterogeneous CatalysisHeterogeneous Catalysis

Ziegler-Natta Catalysts

Homogeneous Homogeneous CatalysisCatalysis

Homogenous catalysts are used when selectivity is critical and product-catalyst separation problems can be solved.

Advantages :

Relatively high specificity

Relatively low reaction temperatures

far more easily studied from chemical & mechanistic aspects

far more active

Generally far more selective for a single product

Disadvantages :o far more difficult for achieving product/catalyst

separations

Catalytic steps in homogeneous reactions

Most catalytic process can be built up from a small number of different types of step– Association / dissociation of a ligand» requires labile complexes– Insertion and elimination reactions– Nucleophilic attack on a coordinated ligand– Oxidation and reduction of a metal center– Oxidative addition / reductive elimination

Wilkinson’s Catalyst:

RhCl(PPh3)3 was the first highly active homogeneous hydrogenation catalyst and was discovered by Geoffrey Wilkinson (Nobel prize winner for Ferrocene) in 1964.

Wilkinson’s Catalyst is a Rh(I) complex, Rh(PPh3)3Cl containing three phosphine ligands and one chlorine.

As a result of the olefin insertion (hydrogen migration) we obtain a Rh (III), 16e-, five coordinate species. A solvent occupies the sixth coordination site to take it to a 18e- species.

Reductive elimination occurs to give the hydrogenated product and the catalytically active species.

Bennett , IC , 1977 , 16 , 665

Olefin Hydrogenation using Wilkinson’s Catalyst

The complex RhCl(PPh3)3 (also known as Wilkinson’s catalyst) became the first highly active homogeneous hydrogenation catalyst that compared in rates with heterogeneous counterparts.

Wilkinson, J. Chem. Soc. (A) 1966, 1711

Hydrogenation mechanism

Steps: (1) H2 addition,(2) alkene addition, (3) migratory insertion, (4) reductive elimination of the alkane, regeneration of the catalyst

Halpern, Chem. Com. 1973, 629; J. Mol. Cat. 1976, 2, 65; Inorg. Chim. Acta. 1981, 50, 11

Wilkinson’s catalyst selectivity

The rate of hydrogenation depends on :(a) presence of a functional group in the vicinity of the C=C bond (b) degree of substitution of the C=C fragment

Hydrogenation is stereoselective:

Wilkinson’s catalyst selectivity

Rh preferentially binds to the least sterically hindered face of the olefin:

Cis-disubstituted C=C react faster than trans-disubstituted C=C:

Wilkinson’s catalyst selectivity

Schneider, JOC 1973, 38, 951

Cationic catalystsCationic catalystsCationic catalysts are the most active homogeneous hydrogenation catalysts developed so far:

Halpern’s mechanism of hydrogenation for cationic Rh catalysts with bidentate phosphines

Steps: (1)alkene addition, (2)(2) H2 addition,(3) migratory insertion, (4) reductive elimination of the alkane, regeneration of the catalyst.

Halpern, Science 1982, 217, 401.

Asymmetric hydrogenationAsymmetric hydrogenation

A variety of bidentate chiral diphosphines have been synthesized and used to make amino acids by hydrogenation of enamides:

Burk, Acc. Chem. Res 2000, 33, 363.

• Synthesis of derivative of L-dihydroxyphenylalanine

Catalysts similar to Wilkinson’s but using chiral phosphine ligands have been used for the asymmetric hydrogenation of small molecules .– Important in the fine chemicals /pharmaceutical industry

Noles and Nyori received the 2001 chemistry Nobel prize for the development of asymmetric hydrogenation catalysis

Chiral hydrogenation catalysts

Knowles, JACS 1975, 97, 2567.

Intermediates in Noyori’s transfer hydrogenation

Lanthanide Hydrogenation Catalysts

Tobin Marks reported the extraordinary activity of (Cp*2LuH)2 for the hydrogenation of alkenes and alkynes. The monometallic complex catalyzes the hydrogenation of 1-hexene with a TOF = 120,000 hr-1 at 1 atm H2, 25ºC!! This is one of the most active hydrogenation catalysts known.

Catalytically active speciesWith bidentate ligands, olefin coordination can precede oxidative addition of H2 (S = methanol, ethanol, acetone).

Halpern, JACS 1977, 99, 8055

Hydroformylation

Hydroformylation was discovered by Otto Roelen in 1938.

The reaction of an alkene with carbon monoxide and hydrogen, catalyzed by cobalt or rhodium salts to form an aldehyde is called hydroformylation.

Heck , JACS,1961,83,4023

Cobalt Phosphine modified catalyst

Cobalt Phosphine catalyst Mechanism

Monsanto Acetic acid Process

1960 basf 1966 monsanto

CATIVA CATIVA ProcessProcess

CATIVA CATIVA ProcessProcess

Wacker Wacker ProcessProcessThis is one of the earliest industrial processes developed in Germany for the conversion of ethylene into acetaldehyde.

Wacker process is more complex than the other catalytic processes described above.

Heterogeneous Heterogeneous CatalysisCatalysis

Heterogeneous catalysts dominate chemical and petrochemical industry: ~ 95% of all chemical processes use heterogenous catalysts.

Ziegler-Natta Catalysis for the Polymerization of olefins

Polymers are large molecules with molecular weights in the range of 104 to 106. These consist of small building units known as monomers

For example polyethylene is made up of ethylene monomersIn all of these cases a single monomer is repeated several times in the polymer chain. The number of repeating units determines the molecular weight of the polymer.

Giulio Natta (1903-1979), an Italian chemist, extended the method to other olefins like propylene and developed variations of the Ziegler catalyst based on his findings on the mechanism of the polymerization reaction.

The German chemist Karl Ziegler (1898-1973) discovered in 1953 that when TiCl3(s) and AlEt3 are combined together they produced an extremely active heterogeneous catalyst for the polymerization of ethylene at atmospheric pressure.

The Ziegler-Natta catalyst family includes halides of titanium, chromium, vanadium, and zirconium, typically activated by alkyl aluminum compounds

Ziegler and Natta received the Nobel Prize in Chemistry for their work in 1963.

There are typically three parts to most polymerizations:

Thanks for your attention


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