Kinetics and Modeling of the Radical Polymerization of Acrylic Acid and of Methacrylic Acid in Aqueous Solution

Total Page:16

File Type:pdf, Size:1020Kb

Kinetics and Modeling of the Radical Polymerization of Acrylic Acid and of Methacrylic Acid in Aqueous Solution Kinetics and Modeling of the Radical Polymerization of Acrylic Acid and of Methacrylic Acid in Aqueous Solution Dissertation zur Erlangung des mathematisch-naturwissenschaftlichen Doktorgrades „Doctor rerum naturalium“ der Georg-August-Universität Göttingen im Promotionsprogramm Chemie der Georg-August University School of Science (GAUSS) vorgelegt von Nils Friedrich Gunter Wittenberg aus Hamburg Göttingen, 2013 Betreuungsausschuss Prof. Dr. M. Buback, Technische und Makromolekulare Chemie, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Prof. Dr. P. Vana, MBA, Makromolekulare Chemie, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Mitglieder der Prüfungskommission Referent: Prof. Dr. M. Buback, Technische und Makromolekulare Chemie, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Korreferent: Prof. Dr. P. Vana, MBA, Makromolekulare Chemie, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Weitere Mitglieder der Prüfungskommission: Prof. Dr. G. Echold, Physikalische Chemie fester Körper, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Prof. Dr. B. Geil, Biophysikalische Chemie, Institut für Physikalische Chemie, Georg-August- Universität Göttingen Jun.-Prof. Dr. R. Mata, Computerchemie und Biochemie,Institut für Physikalische Chemie, Georg-August-Universität Göttingen Prof. Dr. A. Wodtke, Physikalische Chemie I / Humboldt-Professur, Institut für Physikalische Chemie, Georg-August-Universität Göttingen Tag der mündlichen Prüfung: 24.10.2013 Meiner Familie Table of Contents Table of Contents Abstract .......................................................................................................................... 1 1 Introduction ............................................................................................................ 3 2 Theoretical Background ......................................................................................... 7 2.1 General Aspects of Radical Stability and Reactivity ...................................... 7 2.2 Ideal Polymerization Kinetics of Radical Polymerization .............................. 9 2.2.1 Formation of Radicals and Initiation ..................................................... 10 2.2.2 Propagation ............................................................................................. 13 2.2.3 Termination ............................................................................................ 13 2.2.4 Steady State Kinetics ............................................................................. 14 2.3 Additional Reactions...................................................................................... 15 2.3.1 Transfer Reactions to Small Molecules .................................................. 15 2.3.2 Intermolecular Transfer to Polymer ...................................................... 19 2.3.3 Intramolecular Transfer to Polymer – Backbiting ................................ 20 2.3.1 β-Scission Reaction ................................................................................. 24 2.3.2 Retardation and Inhibition .................................................................... 26 2.4 Influences on Rate Coefficients ..................................................................... 27 2.4.1 Temperature and Pressure ..................................................................... 29 2.4.2 Concentration ......................................................................................... 30 2.4.3 Ionization ................................................................................................ 33 2.4.4 Chain Length .......................................................................................... 38 2.4.5 Conversion .............................................................................................. 45 2.5 Computer Modeling of Polymerizations ........................................................ 51 3 Materials, Experimental Procedures and Data Evaluation ................................ 55 3.1 Chemicals ....................................................................................................... 55 V Table of Contents 3.1.1 Monomers ............................................................................................... 55 3.1.2 Solvents .................................................................................................. 57 3.1.3 Initiators ................................................................................................. 58 3.1.4 Inhibitors ................................................................................................ 60 3.1.5 Substances used to prepare Buffer Solutions ........................................ 60 3.1.6 Others ..................................................................................................... 61 3.2 Purification Procedures ................................................................................. 63 3.3 NIR ................................................................................................................ 63 3.3.1 Setup ....................................................................................................... 63 3.3.2 Thermally initiated Polymerization in a Cuvette.................................. 64 3.3.3 Photoinitiated Polymerization in a Cuvette .......................................... 65 3.3.4 Degree of Monomer Conversion ............................................................. 65 3.4 EPR ................................................................................................................ 69 3.4.1 Setup ....................................................................................................... 69 3.4.2 Organic Samples .................................................................................... 69 3.4.3 Aqueous Samples ................................................................................... 70 3.4.1 Deconvolution of Spectra ........................................................................ 70 3.4.2 Calibration .............................................................................................. 70 3.5 NMR ............................................................................................................... 71 3.5.1 Quantitative 1H-NMR ............................................................................ 71 3.5.2 Quantitative 13C-NMR ........................................................................... 72 3.5.3 Polymerization in NMR Sample Tube ................................................... 77 3.6 Density Measurement ................................................................................... 78 3.7 Viscosity Measurement ................................................................................. 78 3.7.1 Important Features of Polymer Solutions ............................................. 79 3.7.2 Polymerization in Viscosity Measurement Capillary ............................ 80 3.8 Preparation of Buffer Solutions .................................................................... 80 3.9 SEC ................................................................................................................ 81 VI Table of Contents 3.10 ESI-MS ........................................................................................................... 81 3.11 HPLC ............................................................................................................. 81 3.12 pH-Meter ........................................................................................................ 82 3.13 High-Temperature Polymerizations.............................................................. 83 3.13.1 Stopped-Flow experiments in High-Pressure Cell ................................. 84 3.13.2 Polymerization in a Tubular Reactor ..................................................... 84 3.14 Other Setups for Polymerization ................................................................... 88 3.14.1 1 L Automated Reactor ........................................................................... 88 3.14.2 Polymerization in a Heating Block ........................................................ 89 3.14.3 Polymerization in a Flask ...................................................................... 89 3.14.4 Polymerization in a Lined Flask ............................................................ 90 3.15 Computer Programs ...................................................................................... 90 3.15.1 Curve Fitting .......................................................................................... 90 3.15.2 Determination of Joint Confidence Regions .......................................... 90 3.15.3 Simulation .............................................................................................. 91 3.16 Error Estimate ............................................................................................... 91 4 Methacrylic Acid ................................................................................................... 95 4.1 Chain-Transfer to 2-Mercaptoethanol .......................................................... 96 4.1.1 Chain Transfer Constants deduced by the Mayo Method ..................... 97 4.1.2 Chain Transfer Constants deduced by the CLD Method .................... 101 4.1.3 Comparison of Mayo and CLD methods .............................................. 103 4.2 Model development for Non-ionized
Recommended publications
  • 1 050929 Quiz 1 Introduction to Polymers 1) in Class We Discussed
    050929 Quiz 1 Introduction to Polymers 1) In class we discussed a hierarchical categorization of the terms: macromolecule, polymer and plastics, in that plastics are polymers and macromolecules and polymers are macromolecules; but all macromolecules are not polymers and all polymers are not plastics. a) Give an example of a macromolecule that is not a polymer. b) Give an example of a polymer that is not a plastic. c) Define polymer. d) Define plastic. e) Define macromolecule. 2) In class we observed a simulation of a small polymer chain of 40 flexible steps. The chain was observed to explore configurational space. a) Explain what the phrase "explore configurational space" means. b) Consider the two ends of the chain to be tethered with a separation distance of about 6 extended steps. If temperature were increased would the chain ends push apart or pull together the tether points? Explain why. c) If one chain end is fixed in Cartesian space at x = 0, what are the limits on the x-axis for the other chain end as it explores configurational space? d) What is the average value of the position on the x-axis? dγ 3) Polymer melts are processed at high rates of strain, , in an extruder, injection molder, or dt calander. a) Sketch a typical plot of polymer viscosity versus rate of strain on a log-log plot showing the power-law region and the Newtonian plateau at low rates of strain. b) Explain using this plot why polymers are processed at high rates of strain. c) Using your own words propose a molecular model that could explain shear thinning in polymers.
    [Show full text]
  • Kinetics of Free-Radical Nonbranched-Chain Addition of Hydrogen Atom to Oxygen Molecule
    Silaev MM, J Mod Chem Sci 2018, 1: 003 HSOA Journal of Modern Chemical Sciences Review Article gen concentration has a maximum. From the energetic standpoint Hydrogen Oxidation: possible nonchain pathways of the free-radical oxidation of hydro- gen and the routes of ozone decay via the reaction with the hydroxyl Kinetics of Free-Radical free radical (including the addition yielding the hydrotetraoxyl free radical) in the Earth’s upper atmosphere were considered. Nonbranched-Chain Addition Keywords: Competition; Energy; Hydrogen; Low-reactive hydro- of Hydrogen Atom to Oxygen tetraoxyl free radical; Thermochemical data Molecule Introduction Michael M Silaev* The kinetics of inhibition for nonbranched-chain processes of Chemistry Faculty, Lomonosov Moscow State University, Moscow, Russia saturated free-radical addition to the C=C and C=O double bonds of alkene and formaldehyde molecules, respectively, by low-reac- tive free radicals that can experience delocalization of the unpaired p-electron was first considered in [1]. In these processes a low-reac- tive free radical is formed in the reaction competing with chain prop- agation reactions through a reactive free radical. In the present work the kinetics of inhibition by low-reactive hydrotetraoxyl free radical is considered for the nonbranched-chain process of the addition of a hydrogen atom to one of the two multiply bonded atoms of the oxy- gen molecule yielding a hydroperoxyl free radical. The hydroperoxyl free radical then abstracts the most labile atom from a molecule of the compound being oxidized or decomposes to turn into a molecule of an oxidation product. The only reaction that can compete with these Abstract two reactions at the chain evolution stage is the addition of the per- New reaction scheme is suggested for the initiated non- oxyl radical to the oxygen molecule (provided that the oxygen con- branched-chain addition of hydrogen atoms to the multiple bond of centration is sufficiently high).
    [Show full text]
  • Chapter 8 Ionic Chain Polymerization
    Chapter 8 Ionic Chain Polymerization The carbon–carbon double bond can be polymerized either by free radical or ionic methods. The difference arises because the p-bond of a vinyl monomer can respond appropriately to the initiator species by either homolytic or heterolytic bond breakage as shown in Eq. 8.1. CC CC CC ð8:1Þ Although radical, cationic, and anionic initiators are used in chain polymeri- zations, they cannot be used indiscriminately, since all three types of initiation do not work for all monomers. Monomers show varying degrees of selectivity with regard to the type of reactive center that will cause their polymerization. Most monomers will undergo polymerization with a radical initiator, although at varying rates. However, monomers show high selectivity toward ionic initiators [1]. Some monomers may not polymerize with cationic initiators, while others may not polymerize with anionic initiators. The coordination polymerization requires coordination catalyst to synthesize polymers. It has been used extensively to polymerize high performance polyolefin but seldom used in the polymerization of polar monomer [2]. The detailed mechanisms of coordination polymerization will be discussed in Chap. 9. The various behaviors of monomers toward polymeri- zation can be seen in Table 8.1. The types of initiation that bring about the polymerization of various monomers to high-molecular-weight polymer are indi- cated. Thus, although the polymerization of all monomers in Table 8.1 is ther- modynamically feasible, kinetic feasibility is achieved in many cases only with a specific type of initiation. The carbon–carbon double bond in vinyl monomers and the carbon–oxygen double bond in aldehydes and ketones are the two main types of linkages that undergo chain polymerization.
    [Show full text]
  • Understanding Multivinyl Monomer Photopolymerization Kinetics Through Modeling and GPC Investigation of Degradable Networks
    Polymer 46 (2005) 6226–6234 www.elsevier.com/locate/polymer Understanding multivinyl monomer photopolymerization kinetics through modeling and GPC investigation of degradable networks Tara M. Lovesteada, Jason A. Burdicka,1, Kristi S. Ansetha,b, Christopher N. Bowmana,c,* aDepartment of Chemical and Biological Engineering, University of Colorado, Boulder, CO 80309-0424, USA bHoward Hughes Medical Institute, University of Colorado, Boulder, CO 80309-0424, USA cDepartment of Restorative Dentistry, University of Colorado Health Sciences Center, Denver, CO 80045-0508, USA Received 12 November 2004; received in revised form 10 March 2005; accepted 11 March 2005 Available online 13 June 2005 Abstract Multivinyl monomers that react to form highly crosslinked, biodegradable networks are being developed as scaffolds for tissue engineering and vehicles for drug delivery; however, this work demonstrates their usefulness in characterizing better the complexities of the kinetics and structural evolution during crosslinking photopolymerization. The molecular weight distributions (MWDs) of the degradation products of networks formed through the free radical photopolymerization of multivinyl monomers validate a novel kinetic model to test hypotheses as to the important kinetic mechanisms during crosslinking. The kinetic model, in conjunction with the experimental results for the degradable network, provides insight into the fundamental termination mechanisms (i.e. chain length dependent termination (CLDT), chain transfer to either a unimolecular species or polymer, and the accumulation of persistent radicals) that control the MWD of the backbone kinetic chains throughout the polymerization. Specifically, the importance of CLDT during autoacceleration and the impact of light intensity on the MWD of the backbone kinetic chains are presented. q 2005 Elsevier Ltd.
    [Show full text]
  • 2017-2018 & Syllabus Iii & Iv Semester
    JSS MAHAVIDYAPEETHA JSS SCIENCE AND TECHNOLOGICAL UNIVERSITY SRI JAYACHAMARAJENDRA COLLEGE OF ENGINEERING, MYSURU SCHEME III TO VIII SEMESTER: 2017-2018 & SYLLABUS III & IV SEMESTER: 2017-2018 DEPARTMENT OF POLYMER SCIENCE AND TECHNOLOGY Scheme of Teaching and Examination for B.E (PST) Credit details Semester Credits I 25.0 II 25.0 III 27.0 IV 27.0 V 27.0 VI 27.0 VII 21.0 VIII 21.0 TOTAL 200.0 1 JSS MAHAVIDYAPEETHA JSS SCIENCE & TECHNOLOGY UNIVERSITY, MYSURU SRI JAYACHAMARAJENDRA COLLEGE OF ENGINEERING MYSURU Scheme of Teaching and Examination for B.E (PS&T) III SEMESTER Contact Credits Marks Exam Sl. Subject Teaching hours Course title duration No. code department per L T P Total CIE SEE Total in hours week Engineering Mathematics–III 1 MA310 MAT 4 0 0 4 4 50 50 100 3 (Numerical Methods) Inorganic and 2 PT310 Physical PST 4 0 0 4 4 50 50 100 3 Chemistry Organic 3 PT320 PST 4 0 0 4 4 50 50 100 3 Chemistry Polymer 4 PT330 PST 4 0 0 4 4 50 50 100 3 Chemistry 5 PT340 Thermodynamics PST 3 1 0 4 5 50 50 100 3 Transport Phenomena in 6 PT350 PST 4 0 0 4 4 50 50 100 3 Materials Engineering-I Organic 7 PT36L PST 0 0 1.5 1.5 3 50 00 50 - Chemistry Lab Fluid Mechanics 8 PT37L PST 0 0 1.5 1.5 3 50 00 50 - Lab Constitution of 9 HU310 Humanity - - - 0 2 50 0 50 - India Total 27.0 33 - 750 - 2 JSS MAHAVIDYAPEETHA JSS SCIENCE & TECHNOLOGY UNIVERSITY, MYSURU SRI JAYACHAMARAJENDRA COLLEGE OF ENGINEERING MYSURU Scheme of Teaching and Examination for B.E (PS&T) IV SEMESTER Credits Contact Marks Exam Sl.
    [Show full text]
  • Effect of Light Intensity on the Free-Radical Photopolymerization Kinetics of 2-Hydroxyethyl Methacrylate: Experiments and Simulations T
    Effect of Light Intensity on the Free-Radical Photopolymerization Kinetics of 2-Hydroxyethyl Methacrylate: Experiments and Simulations T. Luu, Z. Jia, Andrei Kanaev, L. Museur To cite this version: T. Luu, Z. Jia, Andrei Kanaev, L. Museur. Effect of Light Intensity on the Free-Radical Photopolymer- ization Kinetics of 2-Hydroxyethyl Methacrylate: Experiments and Simulations. Journal of Physical Chemistry B, American Chemical Society, 2020, 124 (31), pp.6857-6866. 10.1021/acs.jpcb.0c03140. hal-03092617 HAL Id: hal-03092617 https://hal.archives-ouvertes.fr/hal-03092617 Submitted on 4 Jan 2021 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. The Journal of Physical Chemistry B 2020 124 (31), 6857-6866 DOI: 10.1021/acs.jpcb.0c03140 Effect of Light Intensity on the Free Radical Photopolymerization Kinetics of 2-Hydoxyethyl Methacrylate (HEMA): Experiments and Simulations T.T.H. Luu a, Z. Jia a,b, A. Kanaev b, L. Museur a* a) Laboratoire de Physique des Lasers CNRS UMR 7538, Université Sorbonne Paris Nord, F-93430, Villetaneuse, France. b) Laboratoire des Sciences des Procédés et des Matériaux CNRS UPR 3407, Université Sorbonne Paris Nord, F-93430, Villetaneuse, France.
    [Show full text]
  • Kinetics of Different Methods of Polymerization
    Technische Universität Berlin Institut für Chemie Polymerization Technology Karl-Heinz Reichert Reinhard Schomäcker Third Edition SS 2017 Preface This teaching booklet has been written for students attending the Master Program of Polymer Science, established as a joint program by four universities in the cities of Berlin and Potsdam. This text book focuses on fundamental aspects of polymerization reaction engineering. In the development of a polymerization process the type of reactor and its mode of operation are key factors, which not only affect reactor performance and safety, but also to a large extend the quality of the polymeric product. This is due to the fact that polymers are non uniform materials and the degree of non uniformity is affected by chemistry and reaction engineering conditions as well. I hope that the contents of this text book will be of help to those students who will be envolved in large scale synthesis of polymers in times to come. I would like to thank my secretary Veronika Schott for writing the manuscript of this booklet and especially for her patience with respect to numerous changes of the text, which I have made all the time. Thanks also go out to Monika Klein, who drew all the figures presented in this book and Scott Kibride who improved the English language. Finally we would like to thank all my former PhD students and many of our colleagues for some of their scientific results, which we have used in this text book. Karl Heinz Reichert Berlin in October 2002 Reinhard Schomäcker Berlin in April 2017 TABLE OF CONTENTS 1.
    [Show full text]
  • Kinetics of Nonbranched-Chain Processes of the Free-Radical
    Global Journal of Science Frontier Research Chemistry Volume 13 Issue 6 Version 1.0 Year 2013 Type : Double Blind Peer Reviewed International Research Journal Publisher: Global Journals Inc. (USA) Online ISSN: 2249-4626 & Print ISSN: 0975-5896 Kinetics of Nonbranched-Chain Processes of the Free-Radical Addition with Reactions, in Which the 1:1 Adduct Radicals Compete for Interaction with Saturated and Unsaturated Components of the Binary Reaction System By Michael M. Silaev Lomonosov Moscow State University, Russia Abstract - Five reaction schemes are suggested for the initiated nonbranched-chain addition of free radicals to the multiple bonds of the unsaturated compounds. The proposed schemes include the reaction competing with chain propagation reactions through a reactive free radical. The chain evolution stage in these schemes involves three or four types of free radicals. One of them is relatively low-reactive and inhibits the chain process by shortening of the kinetic chain length. Based on the suggested schemes, nine rate equations (containing one to three parameters to be determined directly) are deduced using quasi-steady-state treatment. These equations provide good fits for the nonmonotonic (peaking) dependences of the formation rates of the molecular products (1:1 adducts) on the concentration of the unsaturated component in binary systems consisting of a saturated component (hydrocarbon, alcohol, etc.) and an unsaturated component (olefin, allyl alcohol, formaldehyde, or dioxygen). Keywords : low-reactive radical, autoinhibitor, competetion, energy, hydrogen. GJSFR-B Classification : FOR Code: 030601p Kinetics ofNonbranched-Chain Processes oftheFree-Radical Addition withReactions, in Which the11 Adduct Radicals Compete for Interaction withSaturated andUnsaturated Components oftheBinary Reaction System Strictly as per the compliance and regulations of: © 2013.
    [Show full text]