Investigations pertaining to the rhodium(I)-catalyzed addition of arylboronic acids to (arylsulfonyl)acetonitriles were undertaken. The resulting carbon-carbon bond forming reaction has led to the efficient synthesis of novel stereoselective (Z)-β-sulfonylvinylamines, which upon acidic hydrolysis, afford useful β-keto sulfones possessing a diverse range of aryl and sulfonyl substituents. The synthetic utility of these (Z)-β-sulfonylvinylamines was subsequently explored by generating the corresponding 1-aza-allyl anion equivalents under basic conditions. This interesting anionic intermediate was then introduced to various α,β-unsaturated systems to produce a diverse array of functionalized pyridine derivatives including unsymmetrical polysubstituted pyridines.

Investigations pertaining to the rhodium(I)-catalyzed addition of arylboronic acids to (arylsulfonyl)acetonitriles were undertaken. The resulting carbon-carbon bond forming reaction has led to the efficient synthesis of novel stereoselective (Z)-β-sulfonylvinylamines, which upon acidic hydrolysis, afford useful β-keto sulfones possessing a diverse range of aryl and sulfonyl substituents. The synthetic utility of these (Z)-β-sulfonylvinylamines was subsequently explored by generating the corresponding 1-aza-allyl anion equivalents under basic conditions. This interesting anionic intermediate was then introduced to various α,β-unsaturated systems to produce a diverse array of functionalized pyridine derivatives including unsymmetrical polysubstituted pyridines.

Rhodococcus is an important industrial organism that possesses diverse metabolic capabilities, it also has a unique cell envelope, composed of an outer layer of mycolic acids and glycolipids (free or bound lipids generally linked to the sugar trehalose). Rhodococcus is able to transform nitriles to the corresponding amide by the enzyme Nitrile Hydratase (NHase), therefore rhodococcal cells can be utilized as biocatalysts in the detoxification of nitrile waste water or in the production of industrially important amides such as acrylamide. However, the NHase within the native cells must be stable with high activity. This research examined how NHase activity and stability can be increased in native cells by changing growth media composition, the impact on the rhodococcal cell envelope was also studied. Growth media composition was altered by supplementing different sugars such as fructose, maltose or maltodextrin to replace glucose in rich solid media containing cobalt and urea for induction of NHase. The supplementation of maltose or maltodextrin resulted in significantly higher NHase activities and greater NHase stability at 55„aC. The supplementation of these different sugars was shown to alter cellular and lipid bound trehalose levels, a sugar known to stabilize proteins and a component of the rhodococcal cell envelope. Cells that had higher levels of cellular trehalose had significantly greater NHase stability at 55„aC. The effect of the different sugar supplements and inducers of NHase, such as cobalt, on cell envelope components such as mycolic acids and glycolipids were examined by High Performance Liquid Chromatography (HPLC) and Thin Layer Chromatography (TLC). The results showed that changes in mycolic acids and glycolipids occurred when the cells were grown in the presence of different sugar supplements and when the cells were induced for NHase. Susceptibility of Rhodococcus sp DAP 96253 to different antibiotics was examined to indicate if changes were occurring in the cell envelope. Differences in antibiotic susceptibility were observed when the cells were grown on media with different sugar supplements and when the cells were induced for NHase. In the presence of cobalt Rhodococcus sp DAP 96253 showed a significant increase in sensitivity to antibiotics. Changes in growth media composition influences the cell envelope of Rhodococcus sp DAP 96253 and also affects NHase activity and stability. Therefore, achieving increased enzyme activity and stability is not entirely dependent on the actual enzyme, but is related to other aspects of the cell, such as the cell envelope and metabolites of the cell.

The direct catalytic hydrogenation of nitrile butadiene rubber (NBR) in latex form was studied as a model system for the development of a new latex hydrogenation process for the modification of unsaturated diene-based polymers. NBR is a synthetic rubber of copolymerized acrylonitrile and butadiene produced in latex form by emulsion polymerization. The catalytic hydrogenation of NBR is an important post-polymerization process resulting in a more stable and tougher derivative, hydrogenated NBR (HNBR), which has been widely used in the automotive and oil drilling industry. The present commercial process involves a number of cumbersome steps to obtain solid NBR from the latex and subsequent dissolution of the solid NBR in a large amount of organic solvent followed by solvent recovery after coagulation of the hydrogenated NBR. Since NBR is produced in latex form, it is very desirable to directly hydrogenate NBR in the latex form which will significantly simplify the hydrogenation process and facilitate subsequent applications. As an economical and environmentally benign alternative to the commercial processes based on the hydrogenation of NBR in organic solution, this direct latex hydrogenation process is of special interest to industry. The objective of this project is to develop an efficient catalytic system in order to realize the direct catalytic hydrogenation of NBR in latex form. OsHCl(CO)(O2)(PCy3)2 was initially used as the catalyst to investigate the possibility of hydrogenation of NBR in latex form and to understand the major factors which affect the hydrogenation operation. It was found that an organic solvent which is capable of dissolving or swelling the NBR was needed in a very small amount for the latex hydrogenation using the Os catalyst, and gel occurred in such a catalytic system during hydrogenation. Wilkinson’s catalyst, RhCl(PPh3)3, was then used for the latex hydrogenation in the presence of a small amount of solvent successfully without gel formation. Further investigation found that Wilkinson’s catalyst has a high activity for NBR latex hydrogenation without the use of any organic solvent. The influences of various operation conditions on hydrogenation rate, such as catalyst and polymer concentrations, latex system composition, agitation, reaction temperature and hydrogen pressure, have been investigated. It was found that the addition of triphenylphosphine (TPP) has a critical effect for the hydrogenation of NBR latex, and the hydrogenation rate was mainly controlled by the amount of catalyst which diffused into the polymer particles. In the presence of TPP, NBR latex can be hydrogenated to more than 95% degree of hydrogenation after about 30 hours at 160oC using Wilkinson’s catalyst with a catalyst to NBR rubber ratio of 1 wt%, without the addition of any organic solvent. The apparent activation energy for such NBR latex hydrogenation over the temperature range of 152oC to 170oC was found to be 57.0 kJ/mol. In the present study, it was also found that there are some impurities within the NBR latex which are detrimental to the hydrogenation reaction and are suspected to be water-soluble surfactant molecules. Deliberately designed solution hydrogenation experiments were conducted to study the impurity issue, and proper latex treatment methods have been found to purify the latex before hydrogenation. To improve the hydrogenation rate and to optimize the latex hydrogenation system, water soluble RhCl(TPPMS)3 catalyst (TPPMS: monosulphonated-triphenylphosphine) was used for the latex hydrogenation of NBR. The latex hydrogenation using the water soluble catalyst with TPP can achieve more than 90% degree of hydrogenation within 20 hours at 160oC. Further experiments using RhCl3 with TPP proved that the water soluble RhCl3 can be directly used as a catalyst precursor to generate the catalytic species in situ for the latex hydrogenation, and a stable NBR latex with 96% degree of hydrogenation can be produced without any gel problem within 19 hours of reaction at 160oC. The catalyst mass transport processes for these Rh based catalysts in the latex system were investigated in order to further optimize the solvent-free latex hydrogenation process. While maintaining the emulsified state of the original latex, the direct catalytic hydrogenation of NBR latex can be carried out efficiently without any cross-linking problem to more than 92% degree of hydrogenation within 8 hours at 160oC. As a result of this research project, new latex hydrogenation technologies were successfully developed to fulfill all major requirements for a solvent-free polymer latex hydrogenation route, which is a significant milestone for the improvement of this polymer modification technology. The finding of TPP’s role as the “catalyst mass transfer promoter” is a breakthrough for the research field related to the hydrogenation of unsaturated diene-based polymers in latex form.

The direct catalytic hydrogenation of nitrile butadiene rubber (NBR) in latex form was studied as a model system for the development of a new latex hydrogenation process for the modification of unsaturated diene-based polymers. NBR is a synthetic rubber of copolymerized acrylonitrile and butadiene produced in latex form by emulsion polymerization. The catalytic hydrogenation of NBR is an important post-polymerization process resulting in a more stable and tougher derivative, hydrogenated NBR (HNBR), which has been widely used in the automotive and oil drilling industry. The present commercial process involves a number of cumbersome steps to obtain solid NBR from the latex and subsequent dissolution of the solid NBR in a large amount of organic solvent followed by solvent recovery after coagulation of the hydrogenated NBR. Since NBR is produced in latex form, it is very desirable to directly hydrogenate NBR in the latex form which will significantly simplify the hydrogenation process and facilitate subsequent applications. As an economical and environmentally benign alternative to the commercial processes based on the hydrogenation of NBR in organic solution, this direct latex hydrogenation process is of special interest to industry. The objective of this project is to develop an efficient catalytic system in order to realize the direct catalytic hydrogenation of NBR in latex form. OsHCl(CO)(O2)(PCy3)2 was initially used as the catalyst to investigate the possibility of hydrogenation of NBR in latex form and to understand the major factors which affect the hydrogenation operation. It was found that an organic solvent which is capable of dissolving or swelling the NBR was needed in a very small amount for the latex hydrogenation using the Os catalyst, and gel occurred in such a catalytic system during hydrogenation. Wilkinson’s catalyst, RhCl(PPh3)3, was then used for the latex hydrogenation in the presence of a small amount of solvent successfully without gel formation. Further investigation found that Wilkinson’s catalyst has a high activity for NBR latex hydrogenation without the use of any organic solvent. The influences of various operation conditions on hydrogenation rate, such as catalyst and polymer concentrations, latex system composition, agitation, reaction temperature and hydrogen pressure, have been investigated. It was found that the addition of triphenylphosphine (TPP) has a critical effect for the hydrogenation of NBR latex, and the hydrogenation rate was mainly controlled by the amount of catalyst which diffused into the polymer particles. In the presence of TPP, NBR latex can be hydrogenated to more than 95% degree of hydrogenation after about 30 hours at 160oC using Wilkinson’s catalyst with a catalyst to NBR rubber ratio of 1 wt%, without the addition of any organic solvent. The apparent activation energy for such NBR latex hydrogenation over the temperature range of 152oC to 170oC was found to be 57.0 kJ/mol. In the present study, it was also found that there are some impurities within the NBR latex which are detrimental to the hydrogenation reaction and are suspected to be water-soluble surfactant molecules. Deliberately designed solution hydrogenation experiments were conducted to study the impurity issue, and proper latex treatment methods have been found to purify the latex before hydrogenation. To improve the hydrogenation rate and to optimize the latex hydrogenation system, water soluble RhCl(TPPMS)3 catalyst (TPPMS: monosulphonated-triphenylphosphine) was used for the latex hydrogenation of NBR. The latex hydrogenation using the water soluble catalyst with TPP can achieve more than 90% degree of hydrogenation within 20 hours at 160oC. Further experiments using RhCl3 with TPP proved that the water soluble RhCl3 can be directly used as a catalyst precursor to generate the catalytic species in situ for the latex hydrogenation, and a stable NBR latex with 96% degree of hydrogenation can be produced without any gel problem within 19 hours of reaction at 160oC. The catalyst mass transport processes for these Rh based catalysts in the latex system were investigated in order to further optimize the solvent-free latex hydrogenation process. While maintaining the emulsified state of the original latex, the direct catalytic hydrogenation of NBR latex can be carried out efficiently without any cross-linking problem to more than 92% degree of hydrogenation within 8 hours at 160oC. As a result of this research project, new latex hydrogenation technologies were successfully developed to fulfill all major requirements for a solvent-free polymer latex hydrogenation route, which is a significant milestone for the improvement of this polymer modification technology. The finding of TPP’s role as the “catalyst mass transfer promoter” is a breakthrough for the research field related to the hydrogenation of unsaturated diene-based polymers in latex form.

Commodity and specialty-grade rubbers, such as styrene-butadiene (SBR) or nitrile-butadiene (NBR), are industrially produced in large trains of continuous reactors using an emulsion polymerization process. Both SBR and NBR systems are largely unstudied. Furthermore, the studies that have been published on NBR have been typically limited to issues concerning the characteristics of the product behaviour (i.e. oil/fuel resistance, tensile strength, hardness, compression set). In this work a detailed mathematical model has been developed in order to simulate the industrial production of NBR via emulsion copolymerization of acrylonitrile (AN) and butadiene (Bd) in batch, continuous and trains of continuous reactors. Model predictions include monomer conversion, polymerization rate, copolymer composition, number- and weight-average molecular weights, tri- and tetra-functional branching frequencies, and the number and average size of polymer latex particles. NBR is typically produced at low temperatures (5 to 10 degrees C) using a redox initiation system to generate free radicals. The system is typically composed of three phases, water, polymer particles, and monomer. Surfactants and electrolytes are used to stabilize the particle and monomer phases as polymerization proceeds. Of particular industrial importance, in today's world of tailor-made products, is detailed control over the polymerization reaction. Such control requires a deep understanding of the influence of various reactant feed rates and reactor operating conditions on the process response. In particular, policies to minimize copolymer composition drift and to control molecular weight, polydispersity and chain branching at desirable levels. The model is cast in a dynamic form using ordinary differential equations to describe the change of each species, the average number of particles, total average polymer volume, and the first three leading moments of the molecular weight distribution. With a multiphase system it is necessary to determine the concentration of each component in each phase. For this, a constant partition coefficient approach was adopted, as opposed to a purely thermodynamic approach. Particle generation was modelled considering both micellar and homogeneous mechanisms. Model parameters were obtained from the open literature or arrived at after sensitivity analysis. Simulations starting the reactors full of water, feeding all ingredients to the first reactor and using an average residence time of 60 minutes revealed considerable copolymer drift starting in the forth reactor (33% conversion), and heightened molecular weights and chain branching once the monomer phase disappeared (50% conversion). Further simulations revealed that both copolymer drift and the growth of molecular weight and branching could be controlled through additional feed streams of AN and chain transfer agent to downstream reactors. Furthermore, polymer productivity could be increased by appropriately splitting the total monomer feed between the first couple of reactors in the train.

Commodity and specialty-grade rubbers, such as styrene-butadiene (SBR) or nitrile-butadiene (NBR), are industrially produced in large trains of continuous reactors using an emulsion polymerization process. Both SBR and NBR systems are largely unstudied. Furthermore, the studies that have been published on NBR have been typically limited to issues concerning the characteristics of the product behaviour (i.e. oil/fuel resistance, tensile strength, hardness, compression set). In this work a detailed mathematical model has been developed in order to simulate the industrial production of NBR via emulsion copolymerization of acrylonitrile (AN) and butadiene (Bd) in batch, continuous and trains of continuous reactors. Model predictions include monomer conversion, polymerization rate, copolymer composition, number- and weight-average molecular weights, tri- and tetra-functional branching frequencies, and the number and average size of polymer latex particles. NBR is typically produced at low temperatures (5 to 10 degrees C) using a redox initiation system to generate free radicals. The system is typically composed of three phases, water, polymer particles, and monomer. Surfactants and electrolytes are used to stabilize the particle and monomer phases as polymerization proceeds. Of particular industrial importance, in today's world of tailor-made products, is detailed control over the polymerization reaction. Such control requires a deep understanding of the influence of various reactant feed rates and reactor operating conditions on the process response. In particular, policies to minimize copolymer composition drift and to control molecular weight, polydispersity and chain branching at desirable levels. The model is cast in a dynamic form using ordinary differential equations to describe the change of each species, the average number of particles, total average polymer volume, and the first three leading moments of the molecular weight distribution. With a multiphase system it is necessary to determine the concentration of each component in each phase. For this, a constant partition coefficient approach was adopted, as opposed to a purely thermodynamic approach. Particle generation was modelled considering both micellar and homogeneous mechanisms. Model parameters were obtained from the open literature or arrived at after sensitivity analysis. Simulations starting the reactors full of water, feeding all ingredients to the first reactor and using an average residence time of 60 minutes revealed considerable copolymer drift starting in the forth reactor (33% conversion), and heightened molecular weights and chain branching once the monomer phase disappeared (50% conversion). Further simulations revealed that both copolymer drift and the growth of molecular weight and branching could be controlled through additional feed streams of AN and chain transfer agent to downstream reactors. Furthermore, polymer productivity could be increased by appropriately splitting the total monomer feed between the first couple of reactors in the train.

L’addition nucléophile des réactifs de Grignard sur les nitriles conduit généralement aux cétones après hydrolyse acide. La double addition, menant à des carbinamines tertiaires après traitement, est beaucoup plus difficile et ne s’effectue habituellement qu’avec les organomagnésiens allyliques. Dans ce contexte, nous avons découvert que les organomagnésiens peuvent effectuer une double addition sur la fonction nitrile des acylcyanhydrines, pour fournir des hydroxyamides. Cette réaction est originale par le fait qu’une large gamme d’organomagnésiens peut être utilisée, dans des conditions particulièrement douces. Cette réaction a été appliquée à la synthèse de différents acides α-aminés α,α-disubstitués, par oxydation de la fonction alcool et hydrolyse du motif amide. La divinylglycine a notamment pu être préparée avec un bon rendement. L’addition successive de deux organomagnésiens différents a aussi pu être réalisée, après optimisation des conditions de réaction, pour accéder à des hydroxyamides disymétriques, précurseurs d’acides aminés quaternaires chiraux. Enfin, l’addition des réactifs de Grignard sur les 3-cyano iminocoumarines N-éthoxycarbonylées a été étudiée. Malgré la présence de nombreux sites électrophiles, la réaction est très chimiosélective, et des chromènes originaux substitués en position 4 ont été obtenus. Les propriétés antifongiques et antibactériennes de ces derniers ont été évaluées. / The nucleophilic addition of Grignard reagents on nitriles generally leads to ketones after acidic hydrolysis. The double addition, providing tertiary carbinamines after work-up, is more difficult and usually occurs only with allylic Grignard reagents. In this context, we discovered that Grignard reagents can perform a double addition on the nitrile function of acyl cyanohydrins, to provide hydroxyamides. This reaction is original by the fact that a wide range of Grignard reagents can be used, in particularly mild conditions. This reaction has been applied to the synthesis of different α,α-disubstituted α-aminoacids, by oxidation of the alcohol functionality and hydrolysis of the amide moiety. Especially, divinylglycine has been prepared in good yield. The successive addition of two different Grignard reagents was also carried out, after optimization of reaction conditions, to access unsymmetrical hydroxyamides, which are precursors of chiral quaternary aminoacids. Finally, the addition of the Grignard reagents on N-ethoxycarbonyl 3-cyano-iminocoumarines was studied. Despite the presence of several electrophilic centers, the reaction is highly chemoselective, and novel chromenes displaying substituent on position 4 were obtained. The antifungal and antibacterial properties of these compounds have been evaluated.

No description available.

A new approach to fulminic acid cycloadditions has been developed. At reduced temperatures, fulminic acid is generated in situ and undergoes 1, 3-diploar cycloaddition reactions with dipolarophiles to form isoxazolines and/or its dimers. This procedure represents a novel, safe general method for the one-step generation of fulminic acid, which complements existing potentially explosive protocols.