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
H 2 Ir III
Vaska s Complex and Its Oxidative Addition Reactions
Catalysis 2009 W.H. Freeman
Catalyst Development
Catalyst Development
Inorganic Chemistry Chapter 1: Figure 26.16 Schematic representation of physisorption and chemisorption of Hydrogen on a nickel metal surface Schematic representation of Diverse sites exposed on a Metal surface a) different Exposed planes, edges; b) steps And kinks from irregularities 2009 W.H. Freeman
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)
Hydrogenation of Alkenes: Wilkinson s catalyst and (one of several versions of) the mechanism
Hydrosilation of Terminal Alkenes
Mechanism: H 2 activation prior to olefin addition Mechanism: Olefins add first to cationic catalyst
Wilkinson s Catalyst: Mechanism for Olefin Hydrogenation Pre-catalyst
With the Rh(I) cationic precursor: Olefin adds prior to H 2 oxidative addition.* *This mechanistic route followed by asymmetric Hydrogenation process
Halpern, Science, 1982
Halpern (Science, 1982, p. 401)
Halpern (Science, 1982, p. 401)
from Collman, Stanford
Wacker process: Oxidation of olefins
Inorganic Chemistry Chapter 1: Figure 26.2 Olefin Isomerization 2009 W.H. Freeman
from Collman, Stanford
Hydroformylation:
Hydroformylation : Union Carbide process