Hydrides and Dihydrogen as Ligands: Hydrogenation Catalysis

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Transcription:

Hydrides and Dihydrogen as Ligands: Hydrogenation Catalysis

Synthesis of Organometallic Complex Hydrides Reaction of MCO with OH -, H -, or CH 2 CHR 2 M(CO) n + OH - = M(CO) n-1 (COOH) - = HM(CO) n-1 - + CO 2 M(CO) n + H - = M(CO) n-1 (C(=O)H) - = HM(CO) n-1 - + CO M(CO) n CH 2 CHR 2 = HM(CO) n-1 - + CH 2 =CR 2 + CO Protonation of MCO anion* M(CO) n - + H + = M(CO) n H Hydrogenation of MCO dimer**: M 2 (CO) 2n + H 2 = M(CO) n H Oxidative addition of H 2 to (typically) d 8 metal M(PR 3 ) 3 X + H 2 = M(CO) n X(H) 2 *Oxidative addition of a proton. If a dianion, the resultant MCO hydride will be anionic and may react as a hydride transfer reagent. **The resultant neutral hydride may have acidic characteristics (i.e., the hydrogen may be removed by a base (reductive deprotonation)

Properties of the M-H functionality Stereochemically active M-H distance range (3d transition metals): 1.5-1.7 Ǻ M-H stretch: 2100 1600 cm -1 M-H hydride resonance: typically upfield, -1 to -20 ppm, but little correlation with electron density M-H Bond Dissociation Energy: 60-100 kcal/mol (Contrast M-C BDE of ca. 26-30 kcal/mol Homolytic cleavage can initiate radical chain reactions Acid/Base character: Varies. HCo(CO) 4 is strong acid, pk a <1; HFe(CO) 4 is weak; Cp 2 W(H) 2 forms Lewis Base/Acid adduct with AlMe 3. Proton loss is slow as in carbon-based acids.

Acidity of MCO Hydrides HM(CO) n + OH - H 2 O + M(CO) n - K a HCo(CO) 4 ~2 HCo(CO) 3 PPh 3 1 10-7 HMn(CO) 5 8 10-8 HRe(CO) 5 very weak H 2 Fe(CO) 4 3 10-5 ; 1 10-14 CpCr(CO) 3 H 10-13.3 CpMo(CO) 3 H 10-13.9 CpW(CO) 3 H 10-16.1

The M-H Bond Functionality: Reactivity H M No change in M oxidation state; reverse is β-elimination MH M - + H + Formal reduction of M oxidation state by 2; electron Withdrawing ligands stabilize M + H Oxidation state of M reduced by 1; can yield H 2 or initiate radical rxns M + + H - M oxidation state is unchanged; electron donating ligands stabilize

Hydride Transfer Reactivity HM(CO) n - + RX XM(CO) n - + RH Rate = k 2 [HM - ][RX] Organometallics, 1984, 3, 646

Suppose one protonates the anionic metal hydride of HW(CO) 5-. Is it possible that the resultant H 2 would remain bound to the metal? Heinekey, JACS, 2005, 850-851; Heinekey, JACS, 2006, 2615-2620

The 2 -Dihydrogen as Ligand Story Kubas, JACS, 1984, 10, 451.

The η 2 -H 2 Complexes - Typically d 6, Oh structures of Cr 0, Mo 0, W 0, Fe II, Ru II, Ir III. - Bonding: Delicate Balance Required for Stability M H H M H H M H H Morris, U. Toronto - donor * acceptor M 2+ (H - ) 2 Kubas, LANL H R 3 P O C - Examples of 2 -H 2 complexes W 0 C O Kubas H CO P PR 3 P H H Fe II C N H Morris ++ P P H H + Ph 3 P H Ir III N PPh 3 C Crabtree Crabtree, Yale

Every Molecule Has a Story: The 2 -H 2 Complexes H H O H H + + H H R 3 P C O C W P P R 3 P H Fe Ir PR 3 N PR C P P 3 O C C N H + + H + - H + H H C O R 3 P W PR 3 C O C O H P Fe P C N H P P + H H R 3 P H Ir N PR 3 C + - stability towards H 2 dissociation - oxidative addition to dihydride Kubas, LANL - strong acid - CNH ligand Morris, U. Toronto - resonance forms - H/D exchange Crabtree, Yale

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Hydrogenation of alkenes on supported metal Involves H 2 dissociation and migration of H-atoms to an adsorbed ethene molecule. (Paul Sabatier, 1890) Mechanism: All isotopomers are seen, therefore highly Reversible prior to loss of the ethane. Volcano diagrams relate stability of products on Surface: Temp. for a set rate of release vs. the Enthalpy. Intermediate values of ΔH f, with the rate being a combination of the rate of adsorption and the rate of desorption gives best catalyst. Just right Surface adducts Very weak Surface adducts Very strong Surface adducts The Goldilocks Effect 2009 W.H. Freeman

A Prominent Example of Heterogeneous Hydrogenation Catalysis: Ammonia Synthesis CH 4 + H 2 O 3 H 2 + CO http://www.greenerindustry.org.uk/pages/ammonia/6ammoniapmhab er.htm CO + H 2 O H 2 + CO 2 CO/H 2

500 x 106 tons/year; Known as population detonator http://www.greenerindustry.org.uk/pages/ammonia/6ammoniapmhab er.htm

http://www.greenerindustry.org.uk/pages/ammonia/6ammoniapmhab er.htm

Conditions According to the equation, the equilibrium mixture will contain more ammonia: When the temperature is lower (the reaction is exothermic in the ammonia direction) When pressure is higher (4 moles of reactant gas make 2 moles of product gas) In practice, the equilibrium is run under conditions of moderate temperatures and pressure. Low temperatures affect the equilibrium favorably, but the reaction would be too slow. Very high pressures, though favoring product creation, increase the costs of plant construction, and present a greater risk to plant workers. With the conditions used, a yield of approximately 20-30 % is achieved from each pass over the catalyst. http://www.greenerindustry.org.uk/pages/ammonia/6ammoniapmhab er.htm

Some homogeneous catalytic processes (Adapted from J. Halpern, Inorg. Chim. Acta 1981, 50, 11)

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With the Rh(I) cationic precursor: Olefin adds prior to H 2 oxidative addition.* *This mechanistic route followed by asymmetric Hydrogenation process

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