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Inverse microsuspension polymerisation of aqueous acrylic acid using redox initiators PDF

283 Pages·2017·5.84 MB·English
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Loughborough University Institutional Repository Inverse microsuspension polymerisation of aqueous acrylic acid using redox initiators ThisitemwassubmittedtoLoughboroughUniversity’sInstitutionalRepository by the/an author. Additional Information: • A Doctoral Thesis. Submitted in partial fulfilment of the requirements for the award of Doctor of Philosophy of Loughborough University. Metadata Record: https://dspace.lboro.ac.uk/2134/11572 Publisher: (cid:13)c Zuifang Liu Please cite the published version. This item was submitted to Loughborough University as a PhD thesis by the author and is made available in the Institutional Repository (https://dspace.lboro.ac.uk/) under the following Creative Commons Licence conditions. For the full text of this licence, please go to: http://creativecommons.org/licenses/by-nc-nd/2.5/ .~ Lol;Ighb.orougb ..,Umverslty Pilkington Library .. ..................................... . ~.\':?.) ~ Author/Filing Title .. , ......... .................................................................................................. Accession/Copy No. q Class Mark ......................•........•................ Vol. No ................ . 1 4 JAN ZOOO - 8 JAN Z001 ." I I I 111111111111111111111111 INVERSE MICROSUSPENSION POLYMERISATION OF AQUEOUS ACRYLIC ACID USING REDOX INITIATORS by ZUIFANGLIU A Doctoral Thesis Submitted in partial fulfilment of the requirements for the award of Doctor of Philosophy of the Loughborough University 28 November, 1997 . ,..' .. '" © by Zuifang Liu (1997) ACKNOWLEDGEMENT I am greatly indebted to my supervisor, Professor B. W. Brooks, for his invaluable guidance and continuous encouragement throughout the course of research. I wish to thank Scott Bader Company Limited for the financial support of this project. Thanks must go to Mr. K. Cheasman and Dr. 1. Peard in Scatt Bader Company Limited for the fruitful discussion on the experimental results. I also wish to thank all the technicians in the Department of Chemical Engineering of the University for their kindly help in my research. Special thanks go to Mr. A. Milne for his help in the experimental work; to Mr. D. Smith for his valuable advice in the development of HPLC technique; to Mr. T. Neale for his help in the construction of temperature control system of polymerisation apparatus; to Mr. S. Graver for printing the photographs of SEM and TEM images. Many thanks should go to Mr. J. Bates in IPTME of the University for his help in developing SEM and TEM techniques. SUMMARY In an inverse microsuspension polymerisation initiated by a redox pair, at least one component of the redox pair must be segregated from the monomer initially to restrict the extent of polymerisation before the dispersion is established. Normally, the monomer and the oxidant in aqueous solution are dispersed in an oil phase, and the aqueous reductant is separately added to start polymerisation. Thus, the reaction system initially consists of two types of aqueous drop and the distribution of reactants is heterogeneous in nature. In the literature, no report to date has been found concerning the mechanistic aspects of this polymerisation process. The present work concerns polymerisation of aqueous acrylic acid in drops that are dispersed in a paraffinic oil and stabilised with a non-ionic surfactant. A sodium metabisulphitel potassium bromate redox initiation system is used. Drop mixing in agitated dispersions has been investigated by examining the aqueous drop behaviour in simulation systems using various developed techniques. The evolution of aqueous drop size and size distribution has been characterised throughout the course of polymerisation using a freeze-fracture technique with electron microscope. The variations of polymerisation rate, limiting conversion, final particle size and size distribution have been investigated by altering several key parameters, such as agitation intensity, volume and composition of the aqueous reductant and ways of adding the aqueous reductant. Aqueous polymerisation of acrylic acid in a single phase, initiated by the redox pair, has been also studied and a reaction scheme has been proposed. Kinetic relationships for polymerisations in both an aqueous homogeneous medium and a heterogeneous medium have been obtained and rationalised in terms of mechanism. A new hypothesis for the polymerisation process has been developed which differs from both conventional suspension and emulsion polymerisations. It is believed that the polymerisation takes place in the aqueous drops as a result of continuous simultaneous coalescence and break-up of the different types of aqueous drops. The surfactant has important effects on the course of polymerisation. A preliminary model has been developed for describing this specific polymerisation process. The publications arising from the present project are listed in Appendix VIII. 11 CONTENTS Acknowledgements Summary ii List of Figures ix List of Tables xiv Chapter 1 INTRODUCTION 1 1.1 Definition of Terms 1 1.2 Research Background and Objective 3 1.3 Thesis Organisation 7 Chapter 2 LITERATURE REVIEW 9 2.1 Polymerisation of Acrylic Acid 9 2.2 Redox Initiators 13 2.3 Inverse Heterogeneous Polymerisation 18 2.3.1 Main Components and Their Effects 19 2.3.1.1 Monomer 19 2.3.1.2 Emulsifier (Surfactant, Stabiliser) 21 2.3.1.3 Initiator(s) 26 2.3.1.4 Dispersion Media 28 2.3.1.5 Other Components 30 2.3.2 Mechanism, Kinetics and Modelling 31 2.3.2.1 Polymerisation Using Oil-soluble Single-component Initiator 32 2.3.2.2 Polymerisation Using Water-soluble Single-component Initiator 37 2.3.2.3 Polymerisation Using Redox Initiators 38 2.3.2.4 Inverse Microemulsion Polymerisation 40 2.4 Drop Mixing in Agitated Liquid-liquid Systems 42 Chapter 3 PRELIMINARY INVESTIGATIONS ON DROP BEHAVIOUR IN INVERSE DISPERSION 49 iii 3.1 Introduction 49 3.2 Methodology 50 3.2.1 Optical Microscopy 50 3.2.1.1 Colouring Method 51 3.2.1.2 Acid Indication Method 52 3.2.1.3 Precipitation Method 52 3.2.1.4 Limitation of Optical Microscopy 54 3.2.2 Light Scattering 57 3.2.3 Electron Microscopy 58 3.2.3.1 Transmission Electron Microscopy 58 3.2.3.2 Scanning Electron Microscopy 59 3.2.4 Viscosity Method 61 3.3 Results and Discussion 62 3.3.1 Stability ofInverse Dispersion 62 3.3.2 Addition of Pure Water to Inverse Dispersion 62 3.3.3 Evolution of Drop Size and Its Distribution 64 3.4 Conclusions 66 Chapter 4 POLYMERISATION APPARATUS AND ITS OPERATION 68 4.1 Design of Polymerisation Apparatus 68 4.1.1 Design of Reactor 68 4.1.2 Design of Stirrer and Baffles 70 4.1.3 Temperature Controlling System 78 4.2 Polymerisation in Inverse Microsuspension 80 4.2.1 Materials 80 4.2.2 Inverse Microsuspension Polymerisation Procedure 81 4.3 Polymerisation in Aqueous Solution 82 4.3.1 Materials 82 4.3.2 Aqueous Polymerisation Procedure 83 4.4 Polymerisation Monitoring 83 4.4.1 Determination of Monomer Conversion and Polymerisation Rate 83 4.4.1.1 High Pressure Liquid Chromatography 84 iv

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This item was submitted to Loughborough University's Institutional . 7.3.1. Effect of Polymerisation Temperature. 7.3.2. Effect of Cross-linking Agent .. These are specially important for the production of acrylic polymers .. It can be seen that the intermediate [03S0Cl02]3- could lead to formation
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