초록 ▼

A process of controlling the molecular weight and dispersity of poly(p-ethylphenol) and poly(m-cresol) synthesized enzymatically by varying the composition of the reaction medium. Polymers with low dispersities and molecular weights from 1000 to 3000 are synthesized in reversed micelles and biphasic

A process of controlling the molecular weight and dispersity of poly(p-ethylphenol) and poly(m-cresol) synthesized enzymatically by varying the composition of the reaction medium. Polymers with low dispersities and molecular weights from 1000 to 3000 are synthesized in reversed micelles and biphasic systems. In comparison, reactions in bulk solvents resulted in a narrow range of molecular weights (281 to 675 with poly(p-ethylphenol) in a DMF/water system and 1,400 to 25,000 with poly(m-cresol) in an ethanol/water system). Poly(p-ethylphenol) was functionalized at hydroxyl positions with palmitoyl, cinnamoyl, and biotin groups.

대표청구항 ▼

1. A method for controlling molecular weight and dispersity of a polymer, said polymer being formed by free radical polymerization using enzyme-catalyzed reaction, the method comprising the folling steps:(a) forming a solvent system having a solubility parameter and dielectric constant, said solvent

1. A method for controlling molecular weight and dispersity of a polymer, said polymer being formed by free radical polymerization using enzyme-catalyzed reaction, the method comprising the folling steps:(a) forming a solvent system having a solubility parameter and dielectric constant, said solvent system being a reaction medium for said polymerization, said reaction medium being reverse micellar solvent mixtures, and said reverse mecellar reaction medium being selected from the group consisting of dioctyl sodium sulfosuccinate in isooctane and water with water at different levels, and dioctyl sodium sulfosuccinate with a mixture of chloroform and isooctane, with isooctane varying from 0 to 100%; (b) varying said solubility parameter for controlling growth of polymer chain, and varying said dielectric constant for affecting enzyme activity, said growth of the polymer chain in said solvent system continuing until a desired weight and dispersity are achieved and said polymer separates from the reaction medium; (c) changing said dielectric constant for changing said enzyme activity for controlling the growth of the polymer chain, and thereby controlling the polymer molecular weight and dispersity; (d) adding to the reaction medium an aqueous preparation of an enzyme; (e) adding to the reaction medium and enzyme preparation, a monomer selected from the group consisting of phenols, aromatic amines, and their derivatives to form a reaction mixture; (f) initiating a polymerization reaction by adding dropwise 30% hydrogen peroxide (w/w) (up to about 30% stoichiometric excess) while stirring the reaction mixture; (g) continuing stirring for several hours; (h) centrifuging the precipitate formed; (i) repeated washing of the precipitate for removing any unreacted monomer; and (j) drying the final precipitate under a reduced pressure at 50.degree. C.