Abstract

Two precatalyst separation paradigms will be reviewed. The first involves the biomimetic, methane monoxygenase enzyme (MMO) precatalyst, [Fe2O(η1-H2O)(η1-OAc)(TPA)2]3+ (TPA=tris[(2-pyridyl)methyl]amine), 1 , formed in situ at pH 4.2 from [Fe2O(μ-OAc)(TPA)2]3+, 2 , which was embedded in an amorphous silicate surface modified by a combination of hydrophilic polyethylene oxide and hydrophobic polypropylene oxide, for ease of separation from the products formed. The resulting catalytic assembly was found to be a biomimetic model for the MMO active site within a hydrophobic macroenvironment, allowing alkane functionalization with t- butyl hydroperoxide (TBHP)/O2 in an aqueous reaction medium (pH 4.2). For example, cyclohexane was oxidized to a mixture of cyclohexanone, cyclohexanol, and cyclohexyl-t -butyl peroxide, in a ratio of ~3:1:2. The balance between polyethylene oxide and polypropylene oxide, tethered on the silica surface, was crucial for maximizing the catalytic activity. Moreover, the mechanism for the silica-based catalytic assembly was found to occur via the Haber–Weiss process. The second precatalyst separation paradigm, the use of the fluorous solvents, which is predicated on solubilizing the precatalyst in a fluorocarbon solution, allows the functionalization of alkanes and alkenes, while selective oxidation of alcohols to aldehydes was also possible; both precatalyst and product are in separate solvent phases. A discussion concerning both separation of precatalyst from product approaches will be presented.

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