Poly?methyl methacrylate??PMMA?,also known as acrylic or organic glass,is an industrially important thermoplastic resin.The ordinary PMMA is flammable and has low solvent resistance and low surface hardness to resist abrasion.Stress-cracking occurs in ordinary PMMA under continuous heavy loading,leading to a limited range of application of PMMA.It is found that the heat resistance,abrasion resistance and anti-creep properties of PMMA increase with the increase of molecular weight of PMMA.For example,ultra-high molecular weight PMMA can maintain its tensile strength,bending strength and other mechanical properties over 200oC and still keeps high toughness and good abrasion-resistance.Ultra-high molecular weight PMMA is generally synthesized by either plasma polymerization or suspension polymerization.However,special equipments?e.g.,radio-frequency generators?are required for plasma polymerization.In addition,due to the complicated polymerization mechanism,the toughness and the impact resistance of PMMA from plasma polymerization are deteriorated.On the other hand,suspension polymerization often needs a large quantity of water as continuous phase and produces a lot of deflocculant-containing wastewater,resulting in low productivity,unclear transparency of polymer product and environmental concerns.This work aims to synthesize ultra-high molecular weight PMMA by an organosilane-initiated polymerization of methyl methacrylate?MMA?.The thesis primarily covers the following aspects:1.An ultra-high molecular weight PMMA has been prepared via an organosilane-initiated polymerization of MMA.The effects of MMA/initiator molar ratio,the types of catalyst and initiator,and the reaction atmosphere on the molecular weight of PMMA were investigated.An ultra-high molecular weight PMMA with a number-average molecular weight as high as 4.18?106 Da,a weight-average molecular weight as high as 5.52?106 Da,and a polydisepersity index of 1.32 was obtained under optimal reaction conditions.2.The MMA/initiator molar ratio,the type of the catalyst and initiator,and the reaction temperature were found to have a great influence on the dependence of PMMA molecular weights on reaction time.With the increase of monomer conversion,the number-average of PMMA increased linearly from 34320 Da to224050 Da in the reaction system containing DPS as an initiator and 0.1‰CP relative to monomer amount as a catalyst under the atmosphere of N2.The results suggested that the reaction system was featured with characteristics of“living”/controlled polymerization.3.A kinetic investigation of the polymerization demonstrated that the polymerization rate followed a first-order kinetics with respect to monomer concentration.The polymerization had an apparent activation energy 126.84 kJ/mol with a pre-expotional factor of 1.15×10188 min-1. |