“…Scheme presents the new multistate strategy that is the subject of the present report in which isospecific and aspecific LCCTP processes for 4M1P are pitted against each other within a single reactor using varying equivalents of diethylzinc, ZnEt 2 (DEZ), as a chain transfer agent (CTA) . As with other multistate LCP and LCCTP processes that we have proposed and experimentally validated, in the absence of chain termination, all the desired features of a living polymerization can be retained if the rate and rate constants for reversible group and polymeryl chain transfer between active transition-metal propagators and either dormant species, in the case of LCP, or an excess population of main-group-metal “surrogate” chain growth centers, in the case of LCCTP, are far greater in magnitude than the corresponding kinetic parameters for chain growth occurring at the transition-metal centers. , This includes the ability to have control over the number-average degree of polymerization, DP n , and a very narrow molar mass distribution (MMD), as defined by a dispersity index, Đ (= M w / M n ) ≤ 1.1, where M n and M w are the number-average and weight-average molar mass indices. However, the key advantage of multistate LCP and LCCTP processes lies with introduction of new mechanistic control points that can be manipulated and brought under external control to direct product formation as an infinite variety of different grades with differing properties that formally exist within a spectrum defined by two limiting ends.…”