Macromolecular Reaction Engineering · 2012 · 36 citations · 29 references
EngineeringChemical EngineeringChemistryPolymer ChemistryPolymer EngineeringReaction EngineeringPolymer AnalysisPolymer CharacterizationPolymer ProcessingPolymer SynthesisPolymerization ProcessesPolymerization Reaction EngineeringAxial DispersionContinuous Flow ProcessingContinuous ProcessingFlow Profile CharacterizationPolymer Polydispersity AnalysisPolymerization Scale-upTubular Polymerization Reactors
Abstract Several unit operations are combined in series to form an integrated, continuous polymerization process; namely inline degassing of monomer stock solution prior to reaction, polymerization using the RAFT approach and precipitation after reaction to form a solid polymeric product. The polymerization is conducted at 70–80 °C with reaction times of 30–90 min in a stainless steel tubular flow reactor, yielding poly(acrylamide) at high conversion (typically >90%) and with a low polydispersity of 1.14–1.23. The axial dispersion occurring inside the tubular flow reactor during polymerization is characterized by reaction profiling using a series of NMR samples. The process can be scaled up to a total output of 1.36 kg of polymer per day on this laboratory‐scale reactor. magnified image
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Octave Levenspiel · Industrial & Engineering Chemistry Research · 1999 · 10K citations
Living Radical Polymerization by the RAFT Process
Graeme Moad, Ezio Rizzardo, San H. Thang · Australian Journal of Chemistry · 2005 · 2.2K citations