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이산화탄소/프로필렌옥사이드 공중합용 고활성 촉매 제조방법

Preparation of a Highly Active Catalyst for CO2/Propylene oxide Copolymerization

초록/요약

A highly active catalytic system for CO2/(propylene oxide) copolymerization was prepared based on the concept of a system containing a Lewis acidic metal center and quarternary ammonium salts units. The catalytic system showed high activity (TON >20000; TOF >20000 h-1) even at high temperature and high [epoxide]/[catalyst] ratio and selectively producing a very high molecular-weight copolymer (Mn, 300,000). The catalyst can be easily separated by filtration through a short pad of silica gel to obtain polymer containing negligible amounts of metal residue (1-2 ppm). The separated catalyst can be reused without significant loss in catalytic performance.

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목차

Table of Contents

Chapter 1. Highly Active and Recyclable Catalytic Systems for CO2/(Propylene Oxide)
Copolymerization.......................................................1
1. Introduction............................................................2
2.Result and Discussion.............................................6
2.1SynthesisandCharacterization.................................6
2.2polymerizationstudies............................................8
2.3Catalyst Recovery Strategy....................................11
2.4 Conclusion.........................................................17
3. Experiment Section...............................................17
4. Reference............................................................33
5. Figures................................................................36

Chapter 2. Efficient Synthetic Route for A Highly Active Catalyst for
CO2/(Propylene Oxide) Copolymerization...................59
1. Introduction..........................................................60
2. Result and Discussion...........................................61
3. Experiment Section...............................................65
4. Reference............................................................70
5. Figures................................................................72

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