An evaluation of the effectiveness of continuous thin film processing in a spinning disc reactor for bulk free-radical photo-copolymerisation

Abstract This paper reports on UV-initiated free-radical copolymerisation of vinyl acetate with n -butyl acrylate (VAc-BA) under conditions of thin film flow in a spinning disc reactor (SDR). Almost 40% overall monomer conversion can be achieved in under 5 s under optimised operating conditions in the SDR, with controlled molecular weight properties of the copolymer, highlighting the good levels of mixing in the film. Residence time on the SDR is a limiting factor in the extent of conversion achievable in a single pass. Comparison with a static film demonstrates the superiority of the SDR in maintaining a high overall rate of polymerisation. Composition of the copolymer formed in the SDR indicates that, due to its plug flow behaviour, the SDR cannot address the inherent problem of compositional drift. We have shown that efficiency of light absorption is dictated by conditions favouring longest UV exposure times, rather than thinner films on the disc. Initiator decomposition efficiency, an important consideration in the overall rate of the co-polymerisation, is enhanced by lower fluid flowrates. This study highlights the promising technology offered by the SDR in combination with UV irradiation for the exploitation of photo-copolymerisation as a viable method for bulk copolymer synthesis.

[1]  Andrew T. Harris,et al.  Review of Major Design and Scale-up Considerations for Solar Photocatalytic Reactors , 2009 .

[2]  M. Dubé,et al.  A systematic approach to the study of multicomponent polymerization kinetics—the butyl acrylate/methyl methacrylate/vinyl acetate example: 1. Bulk copolymerization , 1995 .

[3]  Kamelia Boodhoo,et al.  Process intensification: spinning disk reactor for styrene polymerisation , 2000 .

[4]  G. Oster,et al.  Photopolymerization of vinyl monomers , 1968 .

[5]  Michael Oelgemoeller,et al.  Highlights of Photochemical Reactions in Microflow Reactors , 2012 .

[6]  Majeed S. Jassim,et al.  Thin film solvent‐free photopolymerization of n‐butyl acrylate. I. Static film studies , 2004 .

[7]  P. Fleury Bulk Polymerisation or Copolymerisation in a Novel Continuous Kneader Reactor , 2006 .

[8]  V. Nekkanti,et al.  Continuous Photopolymerization of n-Butyl Acrylate Using a Narrow Channel Reactor , 2008 .

[9]  Kamelia Boodhoo,et al.  Online conductivity measurement of residence time distribution of thin film flow in the spinning disc reactor , 2012 .

[10]  Oskar Nuyken,et al.  The spinning disk reactor: an example of a process intensification technology for polymers and particles , 2012 .

[11]  W. Dominique,et al.  Modelling of a falling thin film deposited photocatalytic step reactor for water purification: Pesticide treatment , 2011 .

[12]  L. Janssen,et al.  Instabilities in free radical polymerization , 2001 .

[13]  G. Geuskens,et al.  Surface modification of polymers - IV. Grafting of acrylamide via an unexpected mechanism using a water soluble photo-initiator , 1996 .

[14]  Lijing Gou,et al.  Modeling of photobleaching for the photoinitiation of thick polymerization systems , 2002 .

[15]  M. Dubé,et al.  Off‐line monitoring of butyl acrylate and vinyl acetate homopolymerization and copolymerization in toluene , 2001 .

[16]  J. Clark,et al.  Classical cationic polymerization of styrene in a spinning disc reactor using silica‐supported BF3 catalyst , 2006 .

[17]  Yildirim H. Erbil Vinyl Acetate Emulsion Polymerization and Copolymerization with Acrylic Monomers , 2000 .

[18]  G. Geuskens,et al.  Surface modification of polymers-III. Photo-initiated grafting of water soluble vinyl monomers and influence on fibrinogen adsorption , 1995 .

[19]  Sabine Beuermann,et al.  Rate coefficients of free-radical polymerization deduced from pulsed laser experiments , 2002 .

[20]  Kamelia Boodhoo,et al.  Catalytic isomerisation of α-pinene oxide to campholenic aldehyde using silica-supported zinc triflate catalysts: II. Performance of immobilised catalysts in a continuous spinning disc reactor , 2007 .

[21]  L. Janssen,et al.  A rheokinetic study of bulk free radical polymerization performed with a helical barrel rheometer , 2004 .

[22]  Simulation of emulsion copolymerization reactions in a continuous pulsed sieve-plate column reactor , 2004 .

[23]  J. Meuldijk,et al.  Production of copolymers with a predefined intermolecular chemical composition distribution by emulsion polymerisation in a continuously operated reactor , 2001 .

[24]  G. R. Meira,et al.  Continuous Bulk Process for the Production of High‐Impact Polystyrene: Recent Developments in Modeling and Control , 2007 .

[25]  James H. Clark,et al.  Handbook of Green Chemistry and Technology , 2002 .