A produção de radicais de carbono \"in vivo\" durante a biotransformação da hidrazina foi demonstrada por ressonância para magnética eletrônica, utilizando o método do captador de spin. Eritrócitos de rato também oxidaram a hidrazina, formando radicais de carbono e nitrogênio, além de espécies reativas de oxigênio. Todas estas espécies, possivelmente formadas \"in vivo\", são potencialmente causadoras de dano a macromoléculas. Podem, por exemplo, iniciar reações secundárias formando radicais de componentes celulares, como ocorreu com a hemoglobina que foi oxidada a radicais tiil-hemoglobina em eritrócitos tratados com hídrazina. Radicais de carbono formados durante a biotransformação da hidrazina em animais expostos provêm necessariamente de substâncias endógenas e podem ser direta ou indiretamente responsáveis pela modificação ( alquilação ) de bases no DNA \"in vivo\". A hidrazona do formaldeído é descrita na literatura como um intermediário da alquilação induzida por hidrazina \"in vivo\". Células L 1210, catalase ou oxihemoglobina de rato foram capazes de formar radicais de carbono durante a oxidação da hidrazona do formaldeído. A oxidação da hidrazona do formaldeído pela catalase foi estudada \"in vítro\" e os radicais de carbono formados, identificados como radicais metila. A base modificada C8 -metil-guanina foi formada em animais expostos, como demonstrado por cromatografia líquida de alta eficiência associada à detecção eletroquímica, sugerindo que ocorreu alquilação do DNA por radicais metila durante a biotransformação da hidrazina \"in vivo\". / The production of carbon-centered radicais during hydrazine biotransformation \"in vivo\" was demonstrated by electron paramagnetic resonance ( EPR ) spin trapping technique. Rat red blood cells also oxidized hydrazine, forming carbon and nitrogen centered radicais, besides oxygen reactive speties. Ali these species, possibly formed \"in vivo\", are potentially harmful to macromolecules. For example, they can initiate secondary reactions in which the radicais from cell components are formed, as it occurred with hemoglobin, forming thiyl-hemoglobin radicais in the red blood cells treated with hydrazine. Carbon-centered radicais produced during the biotransformation of hydrazine in exposed animais must be derived from endogenous sources and may be directly or indirectly responsible for the modificaton ( alkylation ) of DNA bases \"in vivo\". The formaldehyde hydrazone is reported in the literature as an intermediate of hydrazine-induced alkylation \"in vivo\". L1210 cells, catalase and rat hemoglobin were able to produce carbon-centered radicais during the oxidation of the formaldehyde hydrazone. The oxidation of formaldehyde hydrazone by catalase was studied \"in vitro\" and the generated carbon-centered radicais were identified as methyl radicais. The modified base C8 -methylguanine was formed in exposed animais, as demonstrated by high performance liquid chromatography with electrochemical detection, suggesting that DNA alkylation by methyl radicais occurred during hydrazine biotransformation \"in vivo.\"

O presente trabalho apresenta estudos de lesão em biomoléculas (DNA e 2\'-deoxiguanosina) induzida por Cu(III)/tetraglicina (Cu(III)/G4), radicais de óxidos de enxofre (SO3·-, SO4·-, SO5·-), HO· e HSO5-, espécies estas geradas durante a autoxidação de S(IV) na presença de Cu(II)/G4 ou Cu(II) (ausência de tetraglicina) e traços de um segundo íon metálico (Ni(II), Co(II) ou Mn(II)). A formação dos radicais SO3·- e HO· foi detectada pela técnica de ressonância paramagnética eletrônica (EPR). As técnicas de espectrofotometria e dicroísmo circular foram empregadas para avaliar a formação de Cu(III)/G4 em diferentes condições experimentais, na presença e ausência de S(IV), e a interação entre os complexos de cobre (II)/(III) e a molécula de DNA. A eficiência da formação de Cu(III) depende da acidez, concentração de S(IV) e dos tampões utilizados. A lesão no DNA plasmidial pUC19 foi verificada empregando-se a técnica de eletroforese em gel de agarose. A extensão da lesão no DNA depende da acidez, concentração de S(IV), tempo de incubação e da presença de um segundo íon metálico. Usando a técnica de cromatografia líquida de alta eficiência (HPLC) foi possível estudar a oxidação de 2\'-deoxiguanosina a 8-oxo-7,8-dihidro-2\'-deoxiguanosina na presença dos oxidantes fortes gerados durante a autoxidação de S(IV) catalisada por Cu(II)/G4. Um estudo comparativo do efeito de vários íons metálicos evidenciou o sinergismo de Cu(II) e traços de um segundo íon metálico (Ni(II), Co(II) ou Mn(II), complexados ou não com tetraglicina). / The present work presents studies related to biomolecules damage (DNA and 2\'-deoxyguanosine) induced by Cu(III)/tetraglycine (Cu(III)/G4), oxysulfur radicals (SO3·-, SO4·-, SO5·-) and HSO5-, species generated during S(IV) autoxidation in the presence of Cu(II)/G4 or Cu(II) (absence of tetraglycine) and trace level of a second metal ion (Ni(II), Co(II) or Mn(II)). The formation of SO3·- and HO· radicals was detected by electronic paramagnetic resonance technique (EPR). Spectrophotometric and circular dichroism techniques were used to evaluate the Cu(III)/G4 formation in different experimental conditions, in the presence and the absence of S(IV), and the interaction of copper (II)/(III) complexes and DNA molecule. The effectiveness of Cu(III) formation depends on the acidity, S(IV) concentration, and buffers used. The damage on pUC 19 plasmid DNA was verified by agarose gel electrophoresis. The extent on the DNA damage was related to acidity, S(IV) concentration, incubation time and to the presence of a second metal ion. Using the high performance liquid chromatography technique (HPLC) it was possible to study the oxidation of 2\'-deoxyguanosine to 8-oxo-7,8-dihydro-2\'-deoxyguanosine in the presence of strong oxidants generated during the S(IV) autoxidation catalyzed by Cu(II)/G4. A comparative study of the effect of several metal ions showed the synergism of Cu(II) and traces of a second metal ion (Ni(II), Co(II) or Mn(II), as tetraglycine complexes or not).

Dans ce travail de thèse, les radicaux hydroxyles et sulfates, générés par les procédés électro-Fenton et électro-persulfate utilisant une anode en fer, respectivement, ont été utilisés pour la dégradation des édulcorants synthétiques et un colorant azoïque. Les études réalisées sont essentiellement concentrées sur : efficacité de dégradation, mécanismes d'oxydation, schémas de minéralisation et évolution de la toxicité lors de traitement des polluants cibles.1. Le procédé électro-Fenton a montré une grande efficacité dans la dégradation oxydative de l'Aspartame (ASP). La dégradation et la minéralisation sont essentiellement affectées par la concentration du catalyseur (Fe2+) et l'intensité du courant. La constante de vitesse absolue de la réaction d'hydroxylation de l'ASP a été déterminée comme (5,23±0,02) x 109 M-1 s-1. Les acides oxalique, oxamique et maléique ont été identifiés comme sous-produits aliphatiques. La toxicité de la solution (méthode Microtox) augment dans un premier temps et ensuite diminue progressivement lors du traitement.(2) L'édulcorant artificiel Saccarine (SAC) a été efficacement dégradée par procédé électro-Fenton avec anodes DSA, Pt et BDD. Cependant, l'utilisation de l'anode BDD a accéléré significativement la minéralisation de la SAC. Les conditions optimales pour la minéralisation efficace de la SAC étaient: [SAC]: 0,2 mM, [Fe2+] (catalyseur): 0,2 mM, [Na2SO4] (électrolyte): 0,05 M, I (courant): 200 mA et pH: 3. Les acides oxalique, formique et maléique ont été identifiés comme sous-produits aliphatiques. La mesure de la toxicité indique une augmentation en début d'électrolyse (formation des intermédiaires toxiques) et puis une diminution progressive le long du traitement.(3) L'édulcorant artificiel Sucralose (SUC) a été complètement minéralisée en 360 min de traitement par procédé électro-Fenton avec l'anode Pt ou BDD. Le taux de minéralisation est affecté par la concentration de Fe2+ et le courant appliqué. L'efficacité du courant de minéralisation diminue avec l'augmentation du courant de 100 à 500 mA avec les deux anodes. Les acides oxalique, pyruvique, formique et glycolique ont été détectés au cours du processus de minéralisation.(4) Les solutions du colorant azoïque Orange II ont été effectivement décolorées par les radicaux sulfates générés par l'activation électrochimique du peroxydisulfate (PDS) utilisant un catalyseur solide, FeOOH (procédé CE/α-FeOOH/PDS). Le pH initial a peu d'effet sur la décoloration. La méthodologie RSM (Response Surface Methodology) basée sur le modèle Box-Behnken a été appliquée pour analyser les variables expérimentales. Les résultats indiquent que le courant a un effet positif sur la vitesse de décoloration. L'interaction du dosage de l'α-FeOOH et la concentration de PDS ont des effets significatifs. Les résultats d'analyse de variance (ANOVA) ont confirmé que les modèles proposés étaient exactes et fiables pour l'analyse des variables du procédé CE/α-FeOOH/PDS. Le catalyseur solide α-FeOOH a montré une bonne stabilité structurelle et pourrait être réutilisé.(5) Les solutions d'Orange II ont été dégradés par les radicaux sulfates obtenus par le même procédé mais avec catalyseur Fe3O4 : EC/Fe3O4/PDS. La vitesse de décoloration est affecté principalement par : pH initial de la solution, densité du courant, concentration de PDS et dosage de Fe3O4. La solution a été totalement décolorée en 60 min dans les conditions suivantes: [Orange II]0: 25 mg/L, [PDS]: 10 mM, [Fe3O4]: 0,8 g/L, densité du courant (j): 8,4 mA/cm2 et pH initial: 6,0. Les expériences de recyclage ont montré que les particules de Fe3O4 étaient stables et pourraient être réutilisées. Les spectres XPS ont montré la formation de Fe(II) sur la surface des particules de Fe3O4 lors de traitement. Les principaux intermédiaires ont été séparés et identifiés par la technique GC-MS et un schéma plausible de dégradation d'Orange II a été proposé / In this paper, electro-Fenton and sulfate radical-based electro-Fenton-like processes were used to degrade artificial sweeteners and azo dye. The results obtained during the research concern the removal efficiency, the oxidation mechanism, degradation pathway and toxicity evolution of target pollutants.(1) Electro-Fenton process was a effective method for the degradation of ASP in water. The removal and mineralization rate was affected by the Fe2+ concentration and applied current. The absolute rate constant of hydroxylation reaction of ASP was (5.23 ± 0.02) × 109 M–1 S–1. Short-chain aliphatic acids such as oxalic, oxamic and maleic acid were identified as aliphatic intermediates in the electro-Fenton process. The bacteria luminescence inhibition showed the toxicity of ASP solution decreased after it reached a maximum during the first period of the oxidation reaction.(2) Artificial sweetener SAC could be degraded effectively by electro-Fenton process with a DSA, Pt or BDD anode. However, the using of BDD anode could accelerate the mineralization of SAC. The optimal conditions for SAC removal were SAC concentration 0.2 mM, Fe2+ concentration 0.2 mM, Na2SO4 concentration 50 mM, applied current 200 mA and initial pH 3.0. Oxalic, formic, and maleic acid were observed as aliphatic byproducts of SAC during electro-Fenton process. The bacteria luminescence inhibition showed the toxicity of SAC solution increased at the beginning of electrolysis, and then it declined until the end of the reaction.(3) Artificial sweetener Sucralose could be completely mineralized in a 360 min reaction by electro-Fenton process with a Pt or BDD anode. The mineralization rate was affected by the Fe2+ concentration and applied current. The mineralization current efficiency (MCE) decreased with rising applied current from 100 to 500 mA with both Pt and BDD anode. Oxalic, pyruvic, formic and glycolic acids were detected during the oxidation of sucralose.(4) Orange II was effectively decolorized by EC/α-FeOOH/PDS process. The initial pH of Orange II solution had little effect on the decolorization of Orange II. RSM based on Box-Behnken statistical experiment design was applied to analyze the experimental variables. The response surface methodology models were derived based on the results of the pseudo-first-order decolorization rate constant and the response surface plots were developed accordingly. The results indicated the applied current showed a positive effect on the decolorization rate constant of Orange II. The interaction of α-FeOOH dosage and PDS concentration was significant. The ANOVA results confirmed that the proposed models were accurate and reiable for the analysis of the varibles of EC/α-FeOOH/PDS process. The catalystα-FeOOH showed good structural stability and could be reused.(5) Aqueous solutions of Orange II have been degraded effectively in the EC/Fe3O4/PDS process. The decolorization rate was affected by the initial pH of Orange II solution, current density, PDS concentration and Fe3O4 dosage. Orange II can be totally decolorizated in a 60 min reaction when initial Orange II concentration was 25 mg/L, PDS concentration was 10 mM, Fe3O4 dosage was 0.8 g/L, current density was 8.4 mA/cm2 and initial pH was 6.0. Recycle experiments showed Fe3O4 particles were stable and can be reused. XPS spectrum indicated Fe(II) was generated on the surface of Fe3O4 particles after reaction. The main intermediates were separated and identified by GC-MS technique and a plausible degradation pathway of Orange II was proposed

No description available.

Thesis (MSCMedSc (Biomedical Sciences. Medical Physiology))--University of Stellenbosch, 2006. / In this study, we presented data on the role of free radicals in human spermatozoa, particularly in the context of centrifugation and the potential development of defective sperm function. In order to achieve this, methods were developed to directly measure intracellular free radicals in human sperm and the effects of exogenously applied free radicals on sperm function were established. The role of brief and prolonged centrifugation and the associated generation of free radicals was also investigated.

Thesis (MSc)--Stellenbosch University, 2000. / ENGLISH ABSTRACT: Please refer to fulltext for abstract / AFRIKAANSE OPSOMMING: Sien asb volteks vir opsomming

Thesis (MSc)--University of Stellenbosch, 2005. / ENGLISH ABSTRACT: Chemical and molecular tagging agents have illustrated their diversity in a number of different applications. One of the most significant applications includes the use of chemical tagging agents for product registration in industry. Industrial enterprises producing good products need to ensure product authenticity to prevent duplication through piracy and unscrupulous industrialists. Fluorescent probes are chemical compounds that satisfy most of the technical and commercial aspects that are required to be excellent tagging agents. They are generally quick to synthesize, do not affect the product integrity, display little or no impact on the uses of the product or the environment and they can be identified by relatively simple detection procedures. The aim of the present study was to synthesize fluorescent polymers as tagging agents for the paint industry. 7-Hydroxy-2H-chromen-2-one (A1) and 7-hydroxy-4-methyl-2H-chromen-2-one (B1), commercially available fluorescent hydroxyl compounds, were selected as the starting materials. An esterification reaction resulted in the production of 2-oxo-2H-chromen-7-yl acrylate (A2) and 4-methyl-2-oxo-2H-chromen-7-yl acrylate (B2), which are acrylic-type monomers that were required for polymerisation. Studies showed that fluorescence was maintained during the esterification. Copolymers poly(MMA-co-A2), poly(MMA-co-B2), poly(BA-co-A2) and poly(BA-co-B2), synthesized via homogeneous free radical initiated copolymerisation, revealed how copolymer compositions were affected by the feed compositions and the pattern of monomer incorporation over time. This was investigated by following individual monomer consumption rates by 1H-NMR spectroscopy. Fluorescence studies revealed that the fluorescence behaviour of A2 and B2 was maintained during the copolymerisation. Latex particles, with fluorescent behaviour, were synthesized via in situ miniemulsion polymerisation. High molecular weight copolymers with monodisperse particle sizes (nm range) were obtained. A bench-top UV lamp and UV-reflectance studies confirmed the fact that fluorescent latex particles can be identified and quantified respectively, when dispersed in paints that are either free of titanium dioxide or paints that contain titanium dioxide. / AFRIKAANSE OPSOMMING: Die diversiteit van chemiese en molekulêre merkers in ‘n verskeidenheid van toepassings is al telkemale geïllustreer. Een van die mees belangrike toepassings in die industrie is die gebruik van chemiese merkers vir produkregistrasie. Industrieë wat goeie produkte verskaf moet die egtheid van hul produkte kan verseker deur duplikasie via nadruk (Eng: piracy) deur ander te voorkom. Fluoresserende merkers is chemiese stowwe wat aan die meeste van die tegniese en kommersiële vereistes voldoen om as uitstekende merkers te dien. Die sintese van die merkers is gewoonlik nie tydrowend nie, beïnvloed nie die integriteit van die produk nie, het min of geen impak op die gebruike van die produk of die omgewing en kan deur relatief eenvoudige prosedures bepaal word. Die doel van hierdie studie was die sintese van fluoresserendepolimere om as merkers in die verfindustrie te dien. 7-Hidroksie-2H-chromen-2-oon (A1) en 7-hidroksie-4-metiel-2H-chromen-2-oon (B1), fluoresserende hidroksielverbindings wat kommersieël beskikbaar is, is gekies as uitgangstowwe vir die bereiding van die merkers in hierdie studie. ‘n Esterifikasie-reaksie het gelei tot die produksie van 2-okso-2H-chromen-7-ielakrilaat (A2) en 4-metiel-2-okso- 2H-chromen-7-ielakrilaat (B2). Hierdie produkte is tipiese akrilaat-tipe monomere wat benodig word vir polimerisasie. Ondersoeke het getoon dat fluoressensie behoue tydens esterifikasie gebly het. Die kopolimere poli(MMA-ko-A2), poli(MMA-ko-B2), poli(BA-ko-A2) en poli(BA-ko-B2) is deur homogene vry-radikaal-geïnisieerde kopolimerisasie gesintetiseer. Daar is vasgestel hoe die kopolimeersamestelling geaffekteer is deur die samestelling van die reagense (Eng: feed composition) en die patroon van monomeer inkorporasie met tyd. Dit was ondersoek deur die tempo van verbruik van die individuele monomere d.m.v. 1H-KMR spektroskopie te bepaal. Daar is verder vasgestel dat die fluoressensie van A2 en B2 gedurende kopolimerisasie behoue gebly het. Latekspartikels, met fluoressensie gedrag, is via in-situ mini-emulsie-polimerisasie gesintetiseer. Hoë molekulêre massa kopolimere met monodisperse partikelgroottes (in die order van nanometers) is verkry. Deur van ‘n UV-lamp en UV-refleksie studies gebruik te maak is daar bepaal dat fluoresserende latekspartikels in polimere, in verf - wat of titaniumdioksied bevat of geen titaniumdioksied bevat nie -, beide geïdentifiseer and gekwantifiseer kan word.

Thesis (MSc)--Stellenbosch University, 2012. / Please refer to full text for abstract

Thesis (PhD)--Stellenbosch University, 2004. / ENGLISH ABSTRACT: To comply with the ever growing demands for materials with better properties and complex architectures, polymer chemistry has resorted to the use of living free radical polymerization techniques. Despite the structural control some of these techniques offer, major disadvantages do exist. For example, most require ultra-pure reagents, hence only a small fraction of the monomers used in industry can be polymerized in this way. This rendered these new living techniques less advantageous from a commercial point of view. Recently, a revolutionary new living free radical process, namely the reversible addition-fragmentation chain transfer process, or RAFT process, was developed that combines the control over the polymer produced with the robustness and versatility of a free radical process. However, the RAFT process is not without its problems. In some dithioester mediated polymerizations, significant inhibition and rate retardation effects have been observed. Two main opposing opinions have been proposed in recent literature to explain these phenomena observed. The main point of difference between these two groups is the fate of the formed intermediate RAFT radicals, i.e., slow fragmentation of the formed intermediate radicals together with possible reversible intermediate RAFT radical termination, or fast fragmentation of the formed intermediate radicals together with possible irreversible intermediate RAFT radical termination. Between these opposing two groups, there is a difference of six orders of magnitude for the rate of fragmentation of the formed intermediate RAFT radicals. The work presented in this thesis is an attempt to clarify some of the mysteries, i.e., inhibition and rate retardation observed in some RAFT polymerizations. Experimental evidence to support or contradict the theories of the above mentioned two opposing groups was investigated. The concentration-time evolution of the intermediate radical concentration (cy), for styrene and butyl acrylate polymerizations mediated by cumyl dithiobenzoate (COB) at 70°C and 90 °C, was followed via in situ electron spin resonance spectroscopy (ESR). The concentration-time evolution profiles observed were ascribed to the formation of very short chains during the early stages of the reaction. It was also found that the RAFT process is not particularly sensitive to oxygen. The intermediate and propagating radical (cp) concentrations (and their ratio) for the cumyl dithiobenzoate mediated styrene polymerizations were examined by ESR spectroscopy and kinetics. The system showed strong chain length effects in kinetics, assuming all chains were of similar number average molar mass (Mn). However, unusual behavior with respect to existing mechanistic knowledge was observed in other aspects of the system. The central equilibrium "constant" (Keq) was found to be dependent on both temperature and initial reactant concentrations. The observed intermediate radical concentrations were not consistent with predictions based on existing literature models. It was also found that the time dependence of the intermediate radical concentration varies significantly with the type of RAFT agent used. Unexpectedly, intermediate radicals were detected at very long reaction times in the virtual absence of initiator, enhancing the belief of possible reversible termination reactions involving the intermediate radicals. An extra radical (nonpropagating or intermediate) species was observed (via ESR spectroscopy) to form during some reactions. Its concentration increased with time. The combination of data from several analytical techniques provided evidence for the formation of dead chains by the termination of intermediate radicals in the free radical polymerization of styrene, mediated by a cumyl dithiobenzoate RAFT agent, at 84°C. Experiments done focused on the early stages of the reactions, targeting very low final number average molar mass values, with high initiator concentrations. The formation of these terminated chains did not occur to a significant extent until a large fraction of the chains reached a degree of polymerization greater than unity. This corresponded to the occurrence of a maximum in intermediate radical concentration. In situ 1H nuclear magnetic resonance (NMR) and electron spin resonance spectroscopy was used to directly investigate the processes that occur during the early stages (typically the first few monomer addition steps) of an AIBN-initiated reversible addition fragmentation chain transfer polymerization of styrene, in the presence of a cyanoisopropyl dithiobenzoate and cumyl dithiobenzoate RAFT agent, at 70°C and 84 °C respectively. 1H NMR spectroscopy allowed the investigation of the change in concentration of important dithiobenzoate species as a function of time. Identification and concentrations of the radicals present in the system could be inferred from corresponding ESR spectroscopy data. An apparent "inhibition" effect was observed in both the cyanoisopropyl and cumyl dithiobenzoate mediated polymerizations. This effect could be reduced by increasing the reaction temperature to 84 °C. However, the use of cumyl dithiobenzoate as RAFT agent prolonged this effect. This apparent "inhibition" effect was attributed to selective fragmentation of the formed intermediate radicals during the early stages of the reaction, and to different propagation rate coefficients (kp) of the resulting (different) radicals. A change in the equilibrium coefficient for the systems investigated was ascribed to possible progressively decreasing addition and fragmentation rate coefficients of propagating and intermediate radicals formed during the reaction. The increase in intermediate radical concentration, and thus possible intermediate radical termination, was shown to also be a probable cause of the rate retardation observed in the RAFT mediated systems investigated. To conclude, probable causes of the observed inhibition and rate retardation in some dithiobenzoate mediated systems were investigated. It was found that intermediate RAFT radical termination does occurs, albeit reversibly or irreversibly. A maximum in the intermediate radical concentration, and thus possible intermediate radical termination, was seen to occur during the observed rate retardation. An apparent inhibition effect observed was ascribed to a possible change in termination kinetics, the formation of terminated intermediate radical products and a rapidly changing kp of the propagating radicals. / AFRIKAANSE OPSOMMING: Om te voldoen aan die ewig groeiende aanvraag vir materiale met beter eienskappe en komplekse samestellings, is in die polimeerchemie lewende vry-radikaal polimerisasietegnieke ontwikkel. Ten spyte van die feit dat party van die polimerisasie tegnieke die strukuur van die gevormende polimere kan beheer, bestaan daar tog nadele. Die meeste polimerisasie tegnieke benodig ultra suiwer reagense, dus kan net 'n klein fraksie van die monomere wat deur die industrie gebruik word op so 'n manier gepolimeriseer word. Dus, vanuit 'n komersieële oogpunt, is die nuwe lewende polimerisasietegnieke minder voordelig. Onlangs is 'n revolusionere nuwe lewende vry-radikaal polimerisasieproses, naamlike die RAFT-(eng. reversible addition-fragmentation chain transfer process) proses ontwikkel, wat die beheer oor die geproduseerde polimere, kombineer met die robuustheid en veelsydigheid van 'n vry-radikaalproses. Die RAFT proses is egter nie sonder probleme nie. Beduidende inhibisie en vertraging van die polimerisasie tempo is in sommige dithioester-bemiddelde polimerisasies opgemerk. Daar is hoofsaaklik twee opponerende opinies oor die redes vir die inhibisie en vertragings effekte. Die grootste verskil tussen die twee groepe lê in die lot van die gevormde intermediêre radikaal, m.a.w. stadige fragmentasie van die gevormende intermediêre radikale tesame met moontlike onveranderlike intermediêre radikaalterminasie, of vinnige fragmentasie tesame met moontlike omkeerbare intermediêre radikaalterminasie. Tussen die twee groepe, is daar 'n verskil van ses ordegrotes vir die groote van die tempo van fragmentasie van die gevormende intermediêre radikaal. Die werk wat in die tesis weergee word, is 'n poging om sommige van die geheime van die RAFT proses, m.a.w. inhibisie en vertraging van die polimerisasietempo, op te los. Die ondersoek was gerig op eksperimetele bewyse om die teorieë van die twee opponerede groepe of te bevestig of teen te spreek. Die konsentrasie tyd-verandering van die intermediêre radikaal konsentrasie vir stireen- en butielakrilaatpolimerisasie, bemiddeled deur CDB (eng cumyl dithiobenzoate) by 70 oe and 90 oe, is gevolg deur middel van in situ (lat. vir in die oorspronklike plek, m.a.w. binne-in die ESR masjien) elektronspin-resonans (ESR) spektroskopie. Die vorm van die konsentrasie tyd-profiele is toegeskryf aan die vorming van baie kort polimeerkettings gedurende die vroeë reaksietye. Dit is ook bepaal dat die RAFT-proses nie besonder sensitief was vir suurstof nie. Die intermediêre en die propagerende radikaalkonsentrasie (en hulle verhouding) vir die CDB bemiddelde stireen polimerisasies, is bepaal deur middel van elektronspin-resonans spektroskopie en die kinetika van die sisteem. Die kinetika van die sisteem toon 'n sterk afhanklikheid teenoor die lengte van die polimeerkettings, as aanvaar word dat al die kettings dieselfde numeriese gemiddelde molêre massa het. Des nieteenstaande, is egter onverwagte gedrag in ander aspekte van die sisteem opgemerk. Dit was ook gevind dat die sentrale ewewigs-"konstante" (Keq) afhanklik was van die temperatuur en die oorspronklike reaktant konsentrasie. Die bepaalde intermediêre radikaalkonsentrasie het verskil van voorspelde waardes gebaseer op literatuur modelle. Dit is ook gevind dat die intermediêre radikaalkonsentrasie afhanklik is van die tipe RAFT agent wat in die polimerisasie reaksies gebruik word. Intermediêre radikale is onverwags gevind na baie lang reaksietye, wanner verwag is dat die konsentrasie van die afsetter, en dus ook die intermediêre radikale, baie klein sou wees. Dit het die verwagting dat omkeerbare intermediêre radikaalterminasie kan plaasving, versterk. 'n Ekstra radikale spesie, wat gedurende die reaksie vorm en waarvan die konsentrasie groter word met tyd, is ook deur ESR-spektroskopie geidentifiseer. 'n Kombinasie van verskillende skeikundige tegnieke is gebruik om bewyse te kry vir die vorming van dooie kettings wat ontstaan deur middel van intermediêre radikale terminasiereaksies, in die vry-radikaalpolimerisasie van stireen, wat deur 'n CDB RAFT-agent bemiddeled word by 84°C. Eksperimente is gedoen om die reaksie tydens vroeë reaksietye te ondersoek. Baie hoë afsetter konsentrasies is ook gebruik, wat tot uiters lae numeriese gemiddelde molêre massas van die polimeerkettings gelei het. Beduidende konsentrasies van die dooie kettings is eers gevind nadat 'n graad van polimerisasie van groter as een bereik is. Dit het ooreengestem met 'n maksimum in die konsentrasie van die intermediêre radikale. In situ 1H kern magnetiese-resonans (KMR) en electronspin-resonans spektroskopie was gebruik om 'n RAFT proses, wat gedurende die vroeë reaksie tye (tipies gedurende die eerste paar monomeer toevoegingstappe) te bestudeer, wat deur AIBN (eng azo bis(isobutyronitrile)) afgeset word en bestaan uit stireen en CIDB (eng cyanoisopropyl dithiobenzoate) en CDB RAFT agente onderskeidelik, en by 70°C and 84 °C reageer. 1H KMRspektroskopie was gebruik om die veranderinge in die konsentrasie van die belangrike spesies te bepaal. Die identifikasie en konsentrasie van die radikale kon bepaal word deur middel van ESR data. 'n Skynbare 'inhibisie-effek' is waargeneem in die reaksies wat bemiddeled word deur CIDB en CDB. Die effek is verminder toe die reaksietemperatuur verhoog is na 84°C. Die gebruik van CDB as RAFT agent het egter die effek vergroot. Die skynbare 'inhibisie effek' was toegeskryf aan die selektiewe fragmentasie van die intermediêre radikale gedurende die vroeë reaksietye, en aan verskillende propagasie tempokoëffisiënte (kp) van die verskillende radikale. Die veranderlike sentrale ewewigskoëffisiënte is toegeskryf aan die toevoegings en fragmentasie tempokoëffisiënte van die propagerende en intermediêre radikale wat toenemend afneem. Die is ook getoon dat die toename in die konsentrasie van die intermediêre radikale en dus moontlike intermediêre radikale terminasie, 'n oorsaak kan wees van die vertraging van die polimerisasietempo in die RAFT-bemiddelde reaksies. Ter samevatting, die waarskynlike oorsake vir inhibisie en die polimerisasietempo vertraging opgemerk in sekere dithiobenzoaat-bemiddelde sisteme, is ondersoek. Dit was gevind dat intermediêre radikaalterminasie wel kan gebeur, of dit nou omkeerbaar of onveranderlik gebeur. 'n Maksimum in die konsentrasie van die intermediêre radikale, en dus moontlike intermediêre radikaalterminasie, het voorgekom tesame met 'n vertraging in die polimerisasietempo. Die skynbare inhibisie-effek wat opgemerk was kan toegeskryf word aan 'n moontlike verandering in die terminasie kinetika, die formasie van getermineerde intermediêre radikale en 'n vinnig veranderende propagasie tempokoëffisiënt.

Thesis (MSc) -- Stellenbosch University, 1999. / ENGLISH ABSTRACT: A free-radical polymerisation process, which has characteristics of a living polymerisation system, as it is capable of producing polymers of pre-determined molecular masses with a narrow molecular mass distribution, is discussed. It is also possible to make blockcopolymers by adding adding different monomers. The basic objective was to describe, discuss and explain the results of the effects of alkyl iodides as chain transfer agents on the seeded emulsion homo- and co-polymerisation of styrene and butyl acrylate. lodoacetonitrile and 1-phenylethyliodide were used as alkyliodides, acting as degenerative chain transfer agents. First, the effects of these alkyl iodides as chain transfer agents on the molecular mass, molecular mass distribution, glass transition temperature, conversion and particle size for the seeded emulsion polymerisation of styrene were studied. Second, the effects of alkyl iodides as chain transfer agents on the kinetics of radical emulsion polymerisation, especially the average amount of radicals per latex particle, were investigated. Third, the possibility of producing block-copolymers by emulsion polymerisation, using alkyl iodides as chain transfer agents, was investigated. To the best of the author's knowledge, results of work carried out in this study offer the first proof that the "living"/controlled radical polymerisation of styrene, with alkyl iodides as chain transfer agents, can be successfully carried out in emulsion. Addition of different alkyl iodides as chain transfer agents, in different concentrations, led to marked changes in the molecular mass, molecular mass distribution, glass transition temperature, conversion and particle size for the seeded emulsion polymerisation of styrene. The molecular masses of the polystyrene that was produced ranged from 156 to 663 577 while the average molecular mass distribution was below 2. Addition of these alkyl iodides to a seeded styrene polymerisation under zero-one conditions led to an average number of free radicals per latex particle that was greater than 1. A styrene seed latex with functional iodine end-groups was created and was successfully co-polymerised with butyl acrylate to produce a perfect styrene-butyl acrylate block-copolymer. This work has industrial importance as it allows the molecular mass, molecular mass distribution and particle size of polymers to be controlled. These factors are directly related to their micro- and macrostructure of polymers. / AFRIKAANSE OPSOMMING: Die vrye-radikaal polimerisasie proses wat die eienskappe van In lewendige polimerisasie sisteem toon, omdat dit moontlik is om 'n polimeer met voorafbepaalde molekulêre massas en 'n baie klein molekulêre massa verspreiding te berei, is bespreek. Dit is ook moontlik om, deur die byvoeging van 'n tweede monomeer, 'n blok ko-polimere te maak. Die doel was om die effekte wat alkieljodiede as ketlingoordragagente op die "seed" homo- en ko-polimerisasie van stireen en butiel akrielaat gehad het te beskryf en te verklaar. Jodoasetonitriel en 1-fenieletieljodied is gebruik as degeneratiewe kettingoordragagente. Eerstens is die uitwerking van hierdie alkieljodiede as kettingoordragagente op die molekulere massa, molekulere massa verspreiding, glas oorgang temperatuur, opbrengs en partikelgrote van die "seed" emulsie polimerisasie van stireen bestudeer. Tweedens is na die uitwerking van alkiekjodiede op die kinetika van In emulsie radikaal polimerisasie gekyk met spesifieke 1<lem op die gemiddelde aantal radikale per emulsie partikel. Derdens is die moontlikheid om blok ko-polimere te berei ondersoek. Na die beste van die outeur se wete is die resultate van hierdie studie die eerste bewys dat die "Iewendige"/gekontroleerde radikaal polimerisasie van stireen met alkieljodiede as ketlingoordragagente suksesvol in emulsie polimerisasie uitgevoer kan word. Die byvoeging van verskillende alkieljodiede, in verskillende konsentrasies, het aanleiding gegee tot opmerklike veranderinge in die molekulere massa, molekulere massa verspreiding, glas oorgang temperatuur, opbrengs en partikelgrote van die "seed" emulsie polimerisasie van stireen. Die molekulere massas van die bereide polistiereen het gewissel tussen 156 en 663 577 en die gemiddelde molekulere massa verspreiding was onder 2. Byvoeging van die alkieljodiede by die "seed" polimerisasie van stireen onder zero-een toestande het In gemiddelde aantal radikale per emulsie partikel van bo 1 gelewer. In Funksionele "seed" emulsie met jodium eindgroepe was geproduseer na 'n suksesvolle ko-polimerisasie met butiel akrielaat en 'n perfekte stireen-butiel akrilaat kopolimeer is verkry. Hierdie werk het industriele belang aangesien dit die beheer van molekulere massa, molekulere massa verspreiding en partikelgrote moontlik maak wat 'n direkte effek het op die mikro- en makro strukture van die polimeer.