Изучено влияние природы растворителя и магнитного порошка на процесс кристаллизации поливинилиденфторида (ПВДФ). Методам изотермической микрокалориметрии определены энтальпии разбавления ПВДФ в растворителях различной химической природы. Полученные данные использованы для расчета параметров Флори-Хаггинса. Получены полимерные композиционные материалы на основе ПВДФ и порошков никеля и железа. Получены зависимости степени кристалличности композиций и максимумов температур плавления от состава. Изучен их фазовый состав методами инфракрасной спектроскопии и дифференциальной сканирующей калориметрии. / The influence of the nature of the solvent and magnetic powder on the crystallization process of polyvinylidenefluoride (PVDF) has been studied. The enthalpies of dilution of PVDF in solvents of various chemical nature are determined by the methods of isothermal microcalorimetry. Data used to calculate Flory-Huggins parameters. Polymer composite materials based on PVDF and powders of nickel and iron are obtained. The dependences of the degree of crystallinity of the compositions and maxima of the melting points on the composition were obtained. The phase composition was studied using infrared spectroscopy and differential scanning calorimetry.

No / Spheric and anisotropic gold nanoparticles (GNPs) such as rods, stars or nanoprism prepared using hexadecyltrimethyl ammonium bromide (CTAB) as the stabilising agent have received a great deal of interest in the last years. The literature procedures exploited lead to GNPs in aqueous solution. We herein describe a fast, efficient, and cheap method to transfer particles of different shapes from water into toluene solution via ligand exchange (CTAB to dodecanethiol), which was mediated by acetone as a cosolvent. Absorption spectra and TEM-pictures before and after the transfer revealed that the particles survived the transfer intact and without change in shape.

No / Caffeine/oxalic acid 2:1 cocrystal exhibited superior stability to humidity over caffeine, but compressional behavior is not studied yet. To compare compressional properties of caffeine/oxalic acid 2:1 cocrystal obtained by different cocrystallization techniques. Cocrystal was obtained by solvent precipitation and ultrasound assisted solution cocrystallization (USSC) and characterized by X-ray powder diffraction and scanning electron microscopy. Compaction study was carried out at different compaction forces. Compact crushing strength, thickness and elastic recovery were determined. Compaction was in order, caffeine > solvent precipitation cocrystal > USSC cocrystal. Caffeine exhibited sticking and lamination, where solvent precipitation compacts showed advantage. Caffeine and solvent precipitation compacts showed sudden drop in compactability, higher elastic recovery with severe lamination at 20,000 N. This was due to overcompaction. Crystal habit of two cocrystal products was same, but USSC cocrystals were difficult to compact. Uniform needle shaped USSC cocrystals must be difficult to orient in different direction and fracture during compression. Elastic recovery of USSC cocrystals was also more compared to other powders indicating less fracture and poor bonding between particles resulting in poor compaction. Cocrystal formation did not improve compressional property of caffeine. Cocrystals exposed to different crystallization environments in two techniques may have resulted in generation of different surface properties presenting different compressional properties.

Yes / Cocrystals consist of two molecules bonded together in a single crystal lattice giving rise to wide applications including improving solubility of poorly soluble pharmaceuticals. Cocrystallization reaction occurs in the oily phase of liquid–liquid phase separation (LLPS) after it is mixed with coformers. Indomethacin–saccharin cocrystal formation was monitored in situ, and the kinetics of crystallization were determined. The crystallization rates show that the process can be proposed to prevent unwanted oily phase formation during LLPS. / Research Development Fund Publication Prize Award winner, Sep 2022.

published_or_final_version / Education / Master / Master of Education

Fabrication of current generation integrated circuits involves the creation of multilevel copper/low-k dielectric structures during the back end of line processing. This is done by plasma etching of low-k dielectric layers to form vias and trenches, and this process typically leaves behind polymer-like post etch residues (PER) containing copper oxides, copper fluorides and fluoro carbons, on underlying copper and sidewalls of low-k dielectrics. Effective removal of PER is crucial for achieving good adhesion and low contact resistance in the interconnect structure, and this is accomplished using wet cleaning and rinsing steps. Currently, the removal of PER is carried out using semi-aqueous fluoride based formulations. To reduce the environmental burden and meet the semiconductor industry's environmental health and safety requirements, there is a desire to completely eliminate solvents in the cleaning formulations and explore the use of organic solvent-free formulations.The main objective of this work is to investigate the selective removal of PER over copper and low-k (Coral and Black Diamond®) dielectrics using all-aqueous dilute HF (DHF) solutions and choline chloride (CC) - urea (U) based deep eutectic solvent (DES) system. Initial investigations were performed on plasma oxidized copper films. Copper oxide and copper fluoride based PER films representative of etch products were prepared by ashing g-line and deep UV photoresist films coated on copper in CF4/O2 plasma. PER removal process was characterized using scanning electron microscopy and X-ray photoelectron spectroscopy and verified using electrochemical impedance spectroscopy measurements.A PER removal rate of ~60 Å/min was obtained using a 0.2 vol% HF (pH 2.8). Deaeration of DHF solutions improved the selectivity of PER over Cu mainly due to reduced Cu removal rate. A PER/Cu selectivity of ~20:1 was observed in a 0.05 vol% deaerated HF (pH 3). DES systems containing 2:1 U/CC removed PER at a rate of ~10 and ~20 Å/min at 40 and 70oC respectively. A mixture of 10-90 vol% de-ionized water (W) with 2:1 U/CC in the temperature range of 20 to 40oC also effectively removed PER. Importantly, etch rate of copper and low-k dielectric in DES formulations were lower than that in conventional DHF cleaning solutions.

Submitted in fulfillment of the requirements for the degree of Doctor of Technology: Chemistry, Durban University of Technology, Durban, South Africa, 2015. / This thesis forms part of the Council for Scientific and Industrial Research, Forestry and Forest Products Research Centre (CSIR-FFP) biorefinery project which aims at developing and implementing novel industrial processes production of cellulose textile fibres. The focus of this study is to investigate the dissolution of South African Eucalyptus raw (unbleached) and final (bleached) dissolving pulp and saw dust wood in an ionic liquid (IL) 1-ethyl-3-methylimidazolium acetate [Emim][OAc] and the co-solvents [dimethylsulfoxide (DMSO)] or [dimethylformamide (DMF)] mixtures, to obtain regenerated cellulose by the further addition of water and acetone. The IL/co-solvent mixtures were able to dissolve the raw and final pulp samples at 120 ˚C for 6 hours whereas the sawdust wood dissolved in 10 hours. The IL/DMF mixture gave higher cellulose recoveries of 41.88 % for the raw pulp, 49.89 % for the final pulp sample and 32.50 % for sawdust wood while the IL/DMSO mixture gave a recovery of 15.25 % for the raw pulp sample, 36.25 % for the final pulp sample and 17.83 % for the sawdust wood sample. The regenerated cellulose materials were characterized by Fourier Transformer Infrared Spectroscopy (FTIR), Nuclear Magnetic Resonance (NMR), Scanning Electron Microscopy (SEM), Thermo gravimetric Analysis (TGA) and Powder X-Ray Diffraction (pXRD), and compared with a standard microcrystalline of cellulose. It was observed that the FTIR and NMR spectra of the regenerated cellulose and MCC were similar which then indicates that no chemical reaction occurred during the dissolution and regeneration process of cellulose. SEM and X-ray diffraction (XRD) patterns of the results showed that after dissolution the cellulose I (native form), the crystalline structure was completely converted into cellulose II (amorphous) structure, and this was due to the removal of lignin and decrease in cellulose crystallinity. TGA results showed that the regenerated cellulose samples have higher char yields compared to the MCC which is due to the IL remaining in the regenerated cellulose. It was also observed that the addition of the co-solvents decreased the viscosity of the IL mixture, facilitating dissolution of the cellulose that led to additional swelling and reduction of the recalcitrant nature of the cellulose crystalline structure and intermolecular interactions. This led to increased accessibility and dissolution of the cellulose. The findings in this study have the potential to bring ILs closer to applications for biomass technology in particular for an economically viable dissolution method for biomass because ILs have a benefit of being easily separated from the anti-solvent, which provides a simple solution for IL recycle ability and re-use. The novel aspect of this study is: . This is the first study in the South African context to examine the influence of the lignin on the dissolution and regeneration of Eucalyptus sawdust wood and dissolving pulp. / D

L’effort physique a été reconnu comme l’un des déterminants majeurs qui affecte l’absorption pulmonaire et la cinétique des solvants industriels, composés volatils très répandus dans le milieu de travail. L’objectif global de ce projet était de caractériser la relation entre divers niveaux de charge de travail et les concentrations biologiques de l’acétone et du styrène ou de ses métabolites utilisés comme des indicateurs biologiques de l’exposition (IBEs) à ces solvants. Des modèles pharmacocinétiques à base physiologique ont été développés et validés afin de reproduire une exposition professionnelle à l’acétone et au styrène, individuellement et en combinaison, durant une semaine complète de travail (8h/jour, 5 jours). Les simulations ont été effectuées suivant une exposition aux valeurs limite d’exposition (500 ppm et 20 ppm, respectivement) et à des charges de travail de 12,5 W (repos), 25 W et 50 W. Les valeurs prédites par les modèles ont été comparées aux valeurs de référence des IBEs actuels. Le niveau d’acétone dans l’urine obtenu à la fin du dernier quart de travail était 3,5 fois supérieur à la valeur au repos (28 mg/L) pour un effort de 50 W, tandis que les niveaux de styrène dans le sang veineux et de ses métabolites dans l’urine ont augmenté d’un facteur d’environ 3,0 en comparaison avec les valeurs au repos, respectivement de 0,17 mg/L et 144 mg/g créatinine. Pour une co-exposition à des concentrations de 20 ppm de styrène et 200 ppm d’acétone et à une activité physique de 50 W, les simulations ont montré une augmentation de 10% du styrène sanguin et une faible diminution de ses métabolites dans l’urine. Les valeurs simulées par les modèles pour l’acétone ou le styrène montrent que des travailleurs dont la charge de travail équivaut à plus de 25 W sont susceptibles d’avoir des concentrations internes pouvant dépasser les valeurs de référence des IBEs respectifs de ces solvants et peuvent être à risque. Les résultats soulignent ainsi l’importance de tenir compte de la charge de travail dans la détermination d’une valeur de référence pour la surveillance biologique de l’acétone et du styrène. / Workload has been recognized as a major determinant for the pulmonary absorption and the kinetics of industrial solvents, which are volatile compounds largely used in the workplace. This study was undertaken to characterize the relationship between different levels of workload and the biological levels of acetone and styrene or its metabolites used as biological exposure indices (BEIs). Physiologically based pharmacokinetic models were adapted and validated in order to simulate a typical week long occupational exposure (8h/day, 5 days) to acetone and styrene alone or in co-exposure. Simulations were conducted at the current threshold limit values of 500 ppm and 20 ppm, respectively, and under workload levels corresponding to rest (12,5 W), 25 W and 50 W. The predicted values were compared to the current reference value of the BEIs. The end-of-shift level of acetone in urine for a workload of 50 W showed a 3,5-fold increase compared to the value at rest (28 mg/L), whereas the level of styrene in venous blood and its metabolites in urine showed about 3,0-fold increases compared to rest (0,17 mg/L and 144 mg/g creatinine, respectively). Simulations showed that a combined exposure of 20 ppm of styrene with 200 ppm of acetone at 50 W lead to an increase of styrene in blood of 10% of the corresponding level without acetone, while the level of metabolites in urine was slightly decreased. The simulated values for both acetone and styrene showed that workers performing heavy tasks (>25 W) are more likely to present higher internal levels which exceed the current BEIs reference values and may lead to health effects.The models described well the impact of workload on internal exposure and highlighted that workload needs to be taken into account while determining reference values for biological monitoring of acetone and styrene.

La substitution est une méthode de prévention primaire qui permet l’élimination à la source des dangers pour les travailleurs. Une des étapes de la démarche est la comparaison des options afin de procéder au choix final. Divers indices de comparaison, basés sur des paramètres physicochimiques, sanitaires et environnementaux des substances, permettent de guider ce choix. Toutefois, aucune évaluation de ces indices n’a été effectuée dans le cas de la substitution des solvants. Une recherche de développement a été entreprise afin de proposer une méthodologie améliorée de comparaison des solvants. La démarche d’analyse de substitution et la comparaison des options de remplacement à l’aide du rapport de danger de vapeur (« Vapour Hazard Ratio », VHR) ont été appliquées à un cas réel de substitution de solvants en entreprise. Trois indices de potentiel de surexposition (IPS) (VHR, « Måleteknisk Arbejdshygiejnisk Luftbehov » (MAL) et « SUBstitution FACtor » (SUBFAC)) et trois indices globaux de hiérarchisation des dangers (indice air (ψiair), « Indiana Relative Chemical Hazard Score » (IRCHS) et « Final Hazard Score » (FHS)) ont été évalués et comparés à partir de listes de 56 et 67 solvants respectivement. La problématique de la non-idéalité des mélanges a aussi été considérée par rapport aux IPS par l’évaluation et la comparaison de 50 mélanges de solvant. Une méthodologie d’établissement d’une valeur limite d’exposition (VLE), pour les solvants n’en possédant pas, a été développée par modélisation de type relations quantitatives propriété-propriété (QPPR). La modélisation QPPR des VLE, effectuée sur une liste de 88 solvants possédant une VLE, a été effectuée à partir des coefficients de partage octanol:air, octanol:eau, sang:air et des constantes métaboliques. L’étude de cas a montré que l’utilisation du VHR facilitait la comparaison des options, bien qu’elle puisse se heurter à l’absence de VLE. Les indices VHR et SUBFAC ont été identifiés comme des méthodes très proches, caractérisées par une forte corrélation (R=0,99) alors que l’indice MAL se distingue des deux autres IPS par une perte d’information sur la volatilité résultant en une corrélation plus faible avec le VHR (R=0,75). L’impact de la non idealité, évalué par le calcul de coefficients d’activité sur une série de 50 mélanges, a permis d’établir que les ratios entre les indices VHR corrigés et non corrigés variaient entre 0,57 et 2,7, suggérant un facteur de sécurité de cinq lors de la comparaison de mélanges. Les analyses de corrélation et de sensibilité ont montré que les indices de hiérarchisation des dangers différaient de façon importante sur leur prise en compte de paramètres comme la volatilité, les VLE, l’exposition cutanée, l’inflammabilité, la cancérogénicité et les divers paramètres environnementaux. Aucun de ces indices ne peut être recommandé pour la substitution des solvants. Deux modèles QPPR ont été développés afin de prédire des VLE et des VHR, et 61 % et 87 % des VHR prédits variaient respectivement d’un facteur maximal de deux et de cinq par rapport aux VHR calculés. Nos résultats mènent à proposer une démarche améliorée de comparaison en deux étapes. Après un tri selon des critères prioritaires de santé, de sécurité et d’environnement, la comparaison devrait se baser sur le calcul du VHR tout en considérant d’autres paramètres selon la situation concrète de l’entreprise ou du procédé. La comparaison devra tenir compte de la non-idéalité pour les mélanges, et de VLE estimées pour les solvants n’en possédant pas. / Substitution is a primary preventive method which allows the elimination of hazards to workers at the source. One of the steps in substitution analysis is the comparison between options in order to choose the best alternative. Various comparison indices based on physicochemical, health and environmental parameters of substances may facilitate the choice. However, no evaluation of theses indices has been done in the case of solvent substitution. Development research was undertaken in order to propose an improved methodology for solvent substitution. A systematic procedure of solvent substitution was applied to a real workplace case and the comparison between options was made using the Vapour Hazard Ratio (VHR). Three Overexposure Potential Indices (OPIs) (VHR, « Måleteknisk Arbejdshygiejnisk Luftbehov » (MAL) and SUBstitution FACtor (SUBFAC)) and three comprehensive hazard screening indices (air index (ψiair), Indiana Relative Chemical Hazard Score (IRCHS) and Final Hazard Score (FHS)) were evaluated and compared using a list of 56 and 67 solvents respectively. In the case of mixtures, the effect of nonideality on OPIs was also investigated by comparing 50 solvent mixtures. Quantitative property-property relationship (QPPR) models were developed for estimating Occupational Exposure Limits (OELs) for solvents without OELs. QPPR models were made from octanol:air, blood:air and metabolic constants using a list of 88 solvents. The case study showed that the use of the VHR made comparison of replacement options easier, although it was limited by the absence of an OEL for a solvent. VHR and SUBFAC were shown to be close with excellent correlation between the two indices (R=0.99) but a worse correlation was calculated between MAL and VHR (R=0.75). This was attributed to the discrete nature of the volatility parameter in MAL. The impact of nonideality, evaluated by the calculation of activity coefficients on 50 solvent mixtures, resulted in ratios between corrected and non corrected VHRs varying between 0.57 and 2.7, suggesting that a safety factor of five could be used when comparing solvent mixtures. Correlation and sensitivity analysis showed that hazard screening indices differed in the way they integrate key substitution factors such as volatility, OEL, skin exposure, flammability, carcinogenicity and various environmental parameters. No index was found to be suitable for performing solvent substitution. Two QPPR modeling approaches were developed for computing OELs and VHRs; and 61 % and 87 % of the predicted VHRs were within a factor of two and five, respectively, of the calculated VHRs. Our results lead us to propose an improved comparison procedure using a two-tier approach. In the first tier, a selection would eliminate solvent candidates having crucial health, safety and environmental impacts. In the second tier, the comparison would emphasize the VHR but also consider other parameters which are relevant to the specific context. Comparison would also take into account nonideality for mixtures and predicted OELs for solvents without such values.

This study examined the effect of neurotoxic chemical exposures on brain processes using Single Photon Emission Computed Tomography (SPECT). A control group carefully screened for good health and minimal chemical exposures was compared to two groups of patients diagnosed with health problems following exposure to pesticides or to organic solvents.