ATRP requires an alkyl halide or pseudohalide [17] (RÀX) as an initiator and a transition-metal complex (e.g., Cu, [10,18] Ru, [9,19] Fe, [20] Os, [21] Mo, [22] Ni, [23] Re, [24] etc. [2,25] ) as a catalyst. The most common catalysts for ATRP are complexes based on copper(I) halide and nitrogen-based ligands. [2,25] ATRP involves the homolytic cleavage of the RÀX bond by a transition-metal complex activator, Mt m -Y/ Ligand, that reversibly generates an alkyl radical, P n * , and the corresponding higher oxidation state metal halide deactivator, X-Mt m + 1 -Y/Ligand (Scheme 2). P n * can then propagate with a vinyl monomer (M), be deactivated by X-Mt m + 1 -Y/Ligand, or terminate with another P n * , at which point two equivalents of deactivator accumulate as persistent radicals. Radical termination is diminished in controlled polymerizations obeying the persistent radical effect (PRE) [26] as the equilibrium becomes strongly shifted toward the dormant species.The PRE is a particular kinetic feature that provides a self-regulating mechanism in radical reactions. According to the PRE, when two radicals are generated at the same rate (for example from the same source, RÀY) and one of them is persistent (e.g., Y) while the other is transient (R * ), the persistent radical eventually becomes the dominating species in solution due to the self-termination of R * . This has the effect of steering the system toward the cross-termination of the two radicals (i.e., formation of RÀY), strongly inhibiting the self-termination of transient radicals. Therefore, the PRE is a key feature of all CRP techniques based on an activation/deactivation process.Polymerization kinetics and degree of control in ATRP largely depend on the appropriate equilibrium between the activation process (generation of radicals, k act ) and the deactivation process (formation of alkyl halides, k deact ). [25] The rate constants and their ratio (K ATRP = k act /