Thesis (Ph. D.)--University of Texas at Austin, 1999. / Vita. Includes bibliographical references (leaves 243-252). Available also in a digital version from Dissertation Abstracts.

Thesis (Ph. D.)--Chemical and Biomolecular Engineering, Georgia Institute of Technology, 2006. / Jones, Christopher, Committee Chair ; Schork, F. Joseph, Committee Co-Chair ; Weck, Marcus, Committee Member ; Meredith, Carson, Committee Member ; Agrawal, Pradeep, Committee Member.

Dissertation (Ph. D.)--University of Akron, Dept. of Chemical Engineering, 2005. / "August, 2005." Title from electronic dissertation title page (viewed 12/27/2005) Advisor, H. Michael Cheung; Committee members, J. Richard Elliott, Stephanie T. Lopina, A. Dhinojwala, Avraam I. Isayev; Department Chair, Steven S. Chuang; Dean of the College, George K. Haritos; Dean of the Graduate School, George R. Newkome. Includes bibliographical references.

Thesis (Ph. D.)--Lehigh University, 2000. / Includes vita. Includes bibliographical references (leaves 41, 81, 130, 183, 270, 315, 336).

The synthesis of ion containing copolymers by emulsion copolymerization of polar vinyl monomers with ionic vinyl monomers has been studied. The copolymerization of n-butyl acrylate with sodium-pstyrene sulfonate proved to be particularly rapid. With the proper choice of chain transfer agent soluble polymers with enhanced rubbery plateaus have been synthesized. The best conditions for the polymerizations were a reaction temperature of 70°C and reaction times up to 8 hours with TWEEN 20 used as the emulsifier. Analysis of the copolymer composition by UV spectroscopy, and potentionmetric titration was not possible due to the vastly different solubility characteristics of the components of this system. This prevented the use of homopolymer blends as standards for these techniques. The study of the copolymerization kinetics of this system was very difficult due to the coagulation of the polymer latex. The rate of copolymerization was nevertheless shown to be very rapid. The synthesis of the sulfonated styrene monomer by a literature procedure led to the formation of a covalent sulfonamide instead of the desired ionic sulfonate. This product was substantiated by l_H and 13_C NMR infrared, mass spectral, and melting point data. Study of the physical properties of these polymers by differential scanning calorimetry and thermal mechanical analysis showed them to have only a low temperature acrylate glass transition with an enhanced rubbery plateau due to the ionic pseudo crosslinking. Stress-strain measurements showed that this pseudo crosslinking gives enhanced tensile properties (modulus, tensile strength) in the ion-containing polymers. / M.S.

Thesis (MScEng)--Stellenbosch University, 2000. / ENGLISH ABSTRACT: ABSTRACT: A new emulsion (code name: NW 120) has been developed by Plascon on laboratory scale, for application in the paint industry. It is an environmentally friendly emulsion in which no coalescent solvent is used. It also has a core-shell morphology. Research was undertaken to scale-up (industrialize) the emulsion polymerization of NW 120. The use of a suitable pilot plant was investigated. An available bench-scale pilot plant (RCl, Mettler Toledo) was found to be very expensive. The reactors were very small (R:1.8 l) and the reactor set-ups (reactor, baffies and stirrer configuration) were not similar to the industrial size reactors used by Plascon. A fully computer controlled bench-scale pilot plant was subsequently designed and built at a fraction of the cost of the commercially available set-up. The reactor (5 I) was a scale-down replica (geometrically similar) of the industrial size reactors used by Plascon. The reactor was designed to also serve as a calorimeter. Very good control was achieved over the reaction temperature and addition rates of the monomers and catalyst. Heat loss and heat capacity models were derived for a variation in the reaction temperature between 82.5 - 87.5 °c in order to perform accurate energy balances (calorimeter) around the reactor. The accuracy of the calorimeter was verified at a reaction temperature of 85°C, by measuring the heat that evolved when a sodium hydroxide solution was diluted with water. The accuracy of the calorimeter was found to be extremely good. The pilot plant was commissioned with an industrially manufactured emulsion (code name: AE 446), well known to Plascon. The results obtained in the pilot plant reactor were very similar to those obtained for the full-scale manufacturing of AE 446. It was determined that if geometrical similarity between the pilot plant reactor and the industrial size reactor is preserved and if the correct process conditions (stirring speed, reaction temperature and addition rates of the monomers/catalyst) are maintained, then the direct scale-up of the production ofNW 120, from bench-scale to full-scale, would be possible. The reaction conditions were varied over a wide range, in order to find the optimum process conditions. The stirring speed was varied between 150 - 550 rpm. Shear sensitivity was observed at stirring speeds of 450 rpm and higher. The measured physical properties at 550 rpm were found to be unacceptable. The optimum stirring speed for the desired particle size and viscosity was found to lie between 150 rpm and 250 rpm. The reaction temperature was varied between 70 and 90 DC. The optimum reaction temperature was found to lie between 80 and 90 De. It was possible to successfully reduce the monomer addition time, and hence the reaction times, by increasing the addition rate of the monomers/catalyst, from 4 h to 2 ~ h. The method developed by Klein et al. (1996), for the scale-up of the stirring speed of emulsion polymerization reactions was used to determine the equivalent fullscale stirring speed. The scale-up of NW 120 was subsequently conducted at 85 DC, at a stirring speed of 35 rpm and the monomers/catalyst were added over a period of 4 h. The use of reduced reaction times were not considered in the first scale-up run since at that stage it was not clear whether the heat removal capability of the industrial size reactor would be adequate to cope with the increase in the evolved heat, associated with an increase in the addition rates of the monomers/catalyst. Very good results were obtained. The measured physical properties of NW 120 produced in the industrial size reactor were found to be almost exactly the same as in the pilot plant reactor. / AFRIKAANSE OPSOMMING: 'n Nuwe emulsie (kode naam NW 120) is deur Plascon op laboratorium skaal ontwikkel, vir die gebruik in die verfbedryf. Dit is 'n omgewingsvriendelike produk en geen oplosmiddels word gebruik vir die filmvormingsproses nie. Hierdie projek handeloor die opskalering (industrialisering) van die produksie van NW 120. Die gebruik van 'n geskikte loodsaanleg is eers ondersoek. Daar is gevind dat die beskikbare laboratorium skaalloodsaanleg (RCl, Mettler Toledo) baie duur was. Die reaktore is baie klein (:::::1.81). Die reaktoropstellings (reaktor, keerplate en roerder-konfigurasie) is ook nie in ooreenstemming met die industriële grootte reaktore wat deur Plascon gebruik word nie. 'n Ten volle rekenaarbeheerde loodsaanleg is ontwerp en gebou teen 'n breuk van die koste van soortgelyke kommersieel beskikbare opstellings. Die reaktor (5 I) is 'n skaalmodel (geometries gelykvormig) van die industriële grootte reaktore wat deur Plascon gebruik word. Die reaktor word ook aangewend as 'n kalorimeter. Baie goeie beheer oor die reaktortemperatuur, sowel as die toevoertempo's van die monomere en die katalis is verkry. Hitteverlies en hittekapasiteits modelle is afgelei vir variasies in die reaktortemperatuur tussen 82.5 - 87.5 °c om dit moontlik te maak om akkurate energiebalanse te kan opstel (kalorimeter). Die akkuraatheid van die kalorimeter is getoets by 85°C, deur die verdunningswarmte van 'n natriumhidroksiedoplossing te meet. Daar is gevind dat die kalorimeter baie akkuraat is. 'n Industrieel vervaardigde (plaseon) emulsie (kode naam: AB 446) is gebruik om die loodsaanleg in bedryf te stel. Die resultate wat in die loodsaanleg verkry is, was ongeveer dieselfde as die resultate wat in die industriële reaktore verkry word. Hierdie resultate toon dat indien die reaktore geometries gelykvormig is en indien die regte prosestoestande (roerspoed, reaksietemperatuur en toevoertempo's van die monomere/katalis) gebruik word, dit moontlik sou wees om NW 120 direk op te skaal van loodsaanleg tot volskaal. Die reaksietoestande is gevaneer oor 'n wye bereik om die optimum prosestoestande te probeer verkry. Die roerspoed is gevarieer tussen 150 - 550 opm. Daar is gevind dat die emulsie sleur sensitief is bokant 'n roerspoed van 450 opm. Die gemete fisiese eienskappe by 'n roerspoed van 550 opm was onaanvaarbaar. Die optimum roerspoed in terme van partikelgrootte en viskositeit lê tussen 150 en 250 opm. Die reaksietemperatuur is gevarieer tussen 90 - 70°C. Die optimum temperatuur lê tussen 90 - 80 °C. Dit was moontlik om die monomeer-toevoertyd, m.a.w die reaksietyd, te verminder deur die toevoertempo van die monomere/katalis te verhoog, van 4 tot 2 ~ uur. Die metode wat deur Klein et al. (1996) ontwikkel is vir die opskalering van die roerspoed van 'n emulsiepolimerisasie reaksie is gebruik om die ekwivalente roerspoed vir die opskalering te verkry. Die opskalering van NW 120 is uitgevoer by 'n reaksietemperatuur van 85°C en 'n roerspoed van 35 opm. Die monomere/katalis is toegevoer oor 'n tydperk van 4 uur. Die verkorte reaksietyd is nie oorweeg vir die opskaleringslopie nie omdat dit nog nie seker was of die hitteverwydering van die industriële reaktor effektief genoeg sou wees om die verhoging in die reaksiewarmte-ontwikkeling, wat geassosieer word met 'n verhoging in die toevoertempo van die monomere/katalis, te kan verwyder nie. Baie goeie resultate is verkry. Die gemete fisiese eienskappe van NW 120 wat verkry is in die industriële reaktor was ongeveer dieselfde as dié wat verkry is op die loodsaanleg.

The objective of this project was to prepare alkyne-functionalized polymer latexes using surfactant-free emulsion polymerization, and then functionalize these polymer latexes with three quaternary ammonium azides via Cu(I)-catalyzed azide/alkyne cycloaddition (CuAAC) in order to produce antimicrobial polymer latexes. Three quaternary ammonium azides with different linear alkyl chain lengths (C4, C8 and C12) were successfully synthesised in high yield ( > 70%) using established procedures, and their purity determined by elemental analysis, Fourier transform infrared (FTIR) spectroscopy and nuclear magnetic resonance (NMR) spectroscopy. Alkyne-functionalized polymer latexes were prepared via surfactant-free emulsion polymerization using 2,2'-azobis(2-methylpropionamidine)dihydrochloride (AIBA) as initiator, [2-(methaccryloyloxy)ethyl]trimethylammonium chloride (MATMAC) as cationic comonomer, propargyl methacrylate (PMA) to provide the alkyne groups, and for some latexes, ethylene glycol dimethacrylate (EGDMA) as crosslinking comonomer. The effects of temperature and the concentrations of AIBA, MATMAC, PMA and EGDMA on monomer conversion, the rate of polymerization, particle diameter and colloidal stability have been investigated. The studies showed that the very high rates of polymerization were due to high values of the number of radicals per particle (in the range 3-2300). The observations also determined that the reaction conditions required to produce small particles (diameter of 150-350 nm) of narrow size distribution were: 75 oC reaction temperature, AIBA at 0.2 wt% to the total mass of monomer, MATMAC level of smaller or equal to 12 mol% to total monomer (including MATMAC), and EGDMA level of < 2.0 mol% to total monomer (excluding EGDMA). Three series of alkyne-functionalized polymer latexes have been synthesised using these conditions: non-crosslinked (NCL), crosslinked (CL) and core-shell (CS). All the latex particles were functionalized with the three quaternary ammonium azides by CuAAC. Zeta potential analysis, FTIR and Raman spectroscopy analysis confirmed the success of the click reactions. The quantitative analysis of FTIR and Raman spectra showed similar values of conversion of click reaction for both NCL and CL particles, indicating NCL and CL particles have similar swellability. The data also showed that significantly higher click reaction conversions were achieved for CS particles (around 60%) than for NCL/CL particles (less than 40%), which indicates that the click reaction only occurred at the surface of particles and that a higher proportion of alkyne groups are located on the surface of CS particles than on NCL/CL particles. The antimicrobial properties of all QAAs, MATMAC, NCL, CL and CS polymer latexes against E. coli bacteria (ATCC 25922) have been investigated using a modified liquid microdilution method in M9 medium, which was shown not to affect latex colloidal stability. It was found that all the polymer latexes showed much higher antimicrobial activities (MIC 6.5-75 µg ml-1) than many antimicrobial polymers reported recently in the literature (MIC 100-2000 µg ml-1); (Ganewatta, M.S. and C.B. Tang, Controlling macromolecular structures towards effective antimicrobial polymers. Polymer, 2015. 63: p. A1-A29). Polymer latexes with clicked-on QAAs showed significantly higher antimicrobial activities than the original latexes. The magnification of the increase in antimicrobial properties of CS particles after click reaction (~3.5 times) was greater than for NCL/CL particles (~2.5 times), showing that a larger amount of QAAs have been clicked onto the surface of CS particles than NCL/CL particles and that the clicked-on QAAs enhance the antimicrobial activity significantly.

Abstract This work investigates the kinetics of the emulsion polymerization of vinyl acetate. Several aspects of this system have been clarified, including the induced decomposition of persulfate, retardation by oxygen and entry by, and analysis of, the aqueous phase oligomeric radicals. It has been shown that the retardation period observed in the emulsion polymerization of VAc can be explained by the effect of traces of oxygen (< 10-6 M) on the entry efficiency of the initiator-derived aqueous-phase oligomeric radicals. Comparison of rates of polymerization in V and persulfate -initiated polymerizations together with electrospray mass spectrometry of aqueous phase oligomers, has shown that the mechanism for the induced decomposition of persulfate by vinyl acetate is chain transfer to initiator from aqueous-phase oligomeric radicals. A value has been determined for the rate coefficient for transfer to initiator, by fitting literature data to a model based on this mechanism. The reported independence of the rate of polymerization from the monomer concentration in the emulsion polymerization of vinyl acetate has been investigated. Possible explanations for this behaviour have been proposed and tested in this work, by measuring radical-loss rates directly with y-relaxation techniques. Although the Y relaxations were found to be affected by experimental artefacts, it has been demonstrated that rapid exit is not responsible for the high radical-loss rates in this system. The major artefact identified in the y relaxations was the significant effect of relatively small exotherms on relaxation behaviour, Methodologies were developed for correcting affected data and for avoiding exotherms under certain conditions. Arrhenius parameters were determined for the rate coefficient for chain transfer to monomer using the In^M method, which utilises the whole MWD. This section of the work is incomplete, for reasons detailed in chapter 5. However, as a preliminary indication it was found that the frequency factor was 106.38 M-1 s-1 and the activation energy was 38.8 kJ mol-1.

Polyaniline (PAn) is an important conjugated conducting polymer because of its good environmental stability. However, the conductive form of polyanilune is difficult to processed because it is insoluble in common organic solvent. This property limits its processibility and application. In the study, we developed a feasible route for preparing polyaniline/surfactant core-shell latex to solve the insoluble problem. The polyaniline latex was made by emulsion polymerization of aniline monomer, using ionic polymer (poly(4-vinylpyridine)-methanesulfonic acid; P4VP(MSA)) as the surfactant and dopant. And then, the nano-size and core-shell morphologies of polyaniline latex was studied by Transmission electron microscopy (TEM) technique. The best conductivity of polyaniline film is approach to 10-2 S/cm.

The successful production of a wide range of polymer latex products relies on the ability to control the rates of particle nucleation, growth and coagulation in order to maintain control over the particle size distribution (PSD). The development of advanced population balance models (PBMs) has simplified this task at the laboratory scale, but commercialization remains challenging as it is difficult to maintain control over the composition (i.e. spatial distributions of reactant concentration) of larger reactors. The objective of this thesis is to develop and test a combined Computational Fluid Dynamics (CFD) -PBM hybrid modeling framework. This hybrid modeling framework can be used to study the impact of changes in process scale on product quality, as measured by the PSD. The modeling framework developed herein differs from previously-published frameworks in that it uses information computed from species tracking simulations to divide the reactor into a series of interconnected zones, thereby ensuring the reactor is zoned based on a mixing metric. Subsequently, an emulsion polymerization model is solved on this relatively course grid in order to determine the time evolution of the PSD. Examination of shear rate profiles generated using CFD simulation (at varying reactor scales) suggests that, dependent on conditions, mechanically-induced coagulation cannot be neglected at either the laboratory or the commercial scale. However, the coagulation models that are formulated to measure the contributions of both types of coagulation simultaneously are either computationally expensive or inaccurate. For this reason the decision was made to utilize a DLVO-coagulation model in the framework. The second part of the thesis focused on modeling the controlled coagulation of high solids content latexes. POLY3D, a CFD code designed to model the flow of non-Newtonian fluids, was modified to communicate directly with a multi-compartment PBM. The hybrid framework was shown to be well-suited for modeling the controlled coagulation of high solid content latexes in the laminar regime. It was found that changing the size of the reactor affected the latex PSD obtained at the end of the process. In the third part of the thesis, the framework was adapted to work with Fluent, a commercial CFD code, in order to investigate the scale-up of a styrene emulsion polymerization reaction under isothermal conditions. The simulation results indicated that the ability to maintain good control of the PSD was inversely related to the reactor blend time. While the framework must be adapted further in order to model a wider range of polymerization processes, the value of the framework, in obtaining information that would otherwise be unavailable, was demonstrated. / Thesis (Ph.D, Chemical Engineering) -- Queen's University, 2012-05-01 07:09:08.362