1. Improved methods for carrying out the reaction between sodium and acetic anhydride have been presented. Separation of reaction products and quantitative determination have been made easier by means of the improvements. 2. The only products isolated from either room-temperature or high-temperature runs have been sodium acetate and a resinous material believed to be a polymer of diacetyl. No diacetyl has been isolated from the original products of any reaction. 3. Comparison has been made between reactions at room temperature and runs made at high temperatures. Room temperature reactions have been found to give the same products as high-temperature runs but in much smaller amounts. 4. Theoretical discussion of the reaction is presented. A possible mechanism for formation of the resin are proposed. 5. Suggestions for future study of the problem are given. / M.S.

The thesis describes the synthesis and application of various alkynones derived from the bis-Weinreb amide of tartaric acid in the total synthesis of macrolactone natural products. The thesis is divided into three sections. First section of the thesis describes the optimization and generalization of the procedure for the addition of alkynyl Grignard / lithium reagents to the bis-Weinreb amide derived from tartaric acid to yield the mono alkynyl ketones was developed. Application of the formed γ-oxo amides was demonstrated in the synthesis of polyols with varied substitutions particularly the synthesis of 1,2,4-triols was accomplished using Ley’s dithianylation as the key step. Scheme 1: Synthesis of polyols from the bis-weinreb amide of tartaric acid. Application of the strategy to the total synthesis of decanolactone natural products achaetolide and (Z)-isomer of (6S,7R,9R)-6,7-dihydroxy-9-propylnon-4-eno-9-lactone was featured. Section B of the thesis deals with the enantiospecific total synthesis of 14-membered macrolactone Sch 725674. Key reactions in the synthesis include the synthesis of the 1,2,4-triol unit from tartaric acid, olefin cross metathesis and ring closing metathesis. Scheme 4: Enantiospecific total synthesis of Sch 725674. Section C of the thesis describes the enantiospecific synthesis of the C9-C22 fragment of the 28-membered polyene polyol macrolide pentamycin. Although isolated in 1958, total synthesis of this antifungal compound was not reported. In application of the methodology developed, the alkynone prepared from the bis-Weinreb amide was elaborated to the required fragment.

This article presents reaction rate data for the simple hydrolysis of acetic anhydride in the acetonitrile/water and acetone/water cosolvent systems and regression analyses using recently developed thermodynamic rate equations that contain electrostatic and solvent-solute terms. The isomole fraction plots for these reaction systems are linear, and previous theoretical work has shown that the electrostatic term is negligible for such systems. On the other hand, the reaction rates are dependent upon the cosolvent mole fraction, indicating that the solvent-solute term, which is modeled empirically, is significant. The results of the analyses provide the foundation for a paradigm shift away from the emphasis on electrostatic effects to more tenable explanations of kinetic behavior in solvent systems.

The hydrolysis of acetic anhydride is a widely-studied liquid phase reaction studied since 1906. Different approaches have been used to study the kinetics of this reaction. Approaches used by researchers have involved the use of sophisticated experimental set-ups. In this work, the pH technique has been adopted which involves the use of a pH meter to monitor the hydrolysis reaction. Analysis of the hydrolysis reaction has been performed for water/acetone cosolvent systems over a range of temperatures and mole fractions. Eyring analysis was performed under isomole fraction conditions and activation enthalpy, entropy, and Gibbs free energy for hydrolysis of acetic anhydride have been determined. The isomole fraction Eyring plots are linear, because, activation enthalpy and entropy are independent of temperature under these conditions. Activation free Gibbs energy increases with increasing temperature at a constant water mole fraction, while it decreases with increasing water mole fraction at constant temperature.

Neste trabalho são apresentadas estratégias para a estimação, em processos químicos, de estados, parâmetros e covariâncias do ruído de processo e das medidas que são testadas com dados experimentais. Para a estimação de estados e parâmetros foram implementadas desde a técnica mais tradicional, o filtro estendido de Kalman (EKF) até as mais modernas da literatura, como o filtro de Kalman Unscented (UKF) e o Moving Horizon Estimator (MHE). A técnica Autocovariance Least-Squares (ALS) permite a estimação das matrizes de covariância do processo e das medidas a partir dos estados medidos dos processos analisados. Três processos foram analisados com as técnicas citadas: a reação de hidrólise de anidrido acético, o aquecimento de um reator de polimerização completamente carregado (sem iniciador) e por fim oito reações diferentes de polimerização em emulsão. Os resultados mostraram que uma sintonia por tentativa e erro para as matrizes de covariância não apresenta um desempenho adequado. Adicionalmente, o UKF mostra um melhor desempenho, quando comparado com o EKF para o monitoramento de processos de polimerização regime em batelada com covariâncias obtidas através de otimização direta. Quando a estimação da covariância com a técnica ALS é implementada e os resultados utilizados em estimadores estocásticos, o desempenho dos estimadores recursivos melhora consideravelmente. Além disso, o MHE mostrou ser uma ferramenta robusta para o monitoramento do coeficiente global de troca térmica (UA) e do calor gerado pela reação para a polimerização em emulsão em regime semi-contínuo. Finalmente, duas características vantajosas da metodologia proposta devem ser destacadas: a independência em relação ao valor inicial para o estado UA e o fato de um único conjunto de matrizes de covariância (quando obtida pela técnica ALS) poder ser utilizado em reações diferentes, sem necessidade de sintonizar novamente as matrizes para cada reação. / In this work, strategies for state, parameter and covariance estimation in chemical processes are presented and tested with experimental data. For state and parameter estimation techniques have been implemented that spread from the traditional Extended Kalman Filter (EKF) to the most modern techniques from literature, such as the Unscented Kalman Filter (UKF) and the Moving Horizon Estimator (MHE). The Autocovariance Least-Squares technique (ALS) allows the covariance matrices of the process and measurement noise to be estimated based on the measured states of the processes analyzed. Three cases were studied using these techniques: the hydrolysis of acetic anhydride, the warming-up stage of a fully charged polymerization reactor (without initiator) to the desired temperature and finally, eight different emulsion polymerization reaction runs. Results showed that determining covariance matrices by trial and error does not lead to an adequate performance. Additionally, the UKF presents a better performance than the EKF for batch polymerization processes with covariance matrices obtained by direct optimization. When the estimation of the covariance is performed by the ALS technique and they are used in a stochastic estimator, the performance of the recursive estimators is considerably improved. Furthermore, the MHE proved to be a robust tool for monitoring the overall heat transfer coefficient (UA) and the heat of reaction for fedbatch emulsion polymerization. Finally, two positive features of the proposed methodology must be highlighted, its low dependency on the initial state condition of UA and the fact that a unique set of covariance matrices (when obtained by the ALS technique) can be used for different reaction runs, without the necessity of tuning the matrices again for each reaction.

A crescente demanda por produtos poliméricos com propriedades cada vez mais estritas tem forçado o desenvolvimento de técnicas de monitoramento em linha cada vez mais precisas e robustas. Infelizmente, grande parte das principais propriedades poliméricas não são quantificáveis em linha a partir das metodologias analíticas atualmente disponíveis e, portanto, na prática, as propriedades finais dos látices poliméricos são obtidas através da caracterização off line de amostras discretas coletadas do processo, resultando em um tempo de análise longo e indesejado para qualquer algoritmo de controle em tempo real. Por outro lado, como as reações de polimerização são altamente exotérmicas é possível quantificar continuamente a taxa de calor gerado pela reação a partir das medidas de temperatura e do balanço de energia que, por sua vez, pode ser usada para obter importantes informações acerca do estado do processo. Entretanto, esta técnica requer a atualização contínua do coeficiente global de troca térmica ao longo da reação, uma vez que este parâmetro está sujeito a variações temporais significativas. Portanto, o presente trabalho tem por objetivo analisar a viabilidade da aplicação conjunta dos conceitos da calorimetria e dos observadores não-lineares para a estimação dos estados de um processo químico. Para isso, serão analisadas duas reações químicas distintas: a) uma reação de hidrólise de anidrido acético, b) uma reação copolimerização em emulsão. Os resultados obtidos mostraram que essa metodologia é extremamente dependente dos parâmetros de sintonia do observador de estado, inviabilizando o seu uso para o monitoramento em linha de um processo químico. Por outro lado, a aplicação direta do balanço de energia para estimação do calor gerado pela reação, mostrou-se uma forma alternativa simples e viável para a estimação em tempo real dos estados de uma reação de polimerização. / The increasing demand for the production of polymers with more tight properties has placed great emphasis on the development of accurate and robust online monitoring techniques of polymerization reactions. Unfortunately, most of the main characteristics are not measurable online from analytical methodologies currently available and, therefore, in practice, the final properties of polymer latexes are obtained through off line characterization of discrete samples collected from the process, resulting in measurement delay which is undesirable for real-time control. On the other hand, since most of the polymerization reactions are highly exothermic, it is possible to quantify continuously the heat release rate based on temperature measurements and energy balance equations that, in turn, can be used to infer valuable information about the state of process. However, this approach requires up-dating the value of the global heat exchange coefficient through reaction, once this parameter is subject to significant time variations. Therefore, this work aims to examine the feasibility of joint implementation of the concepts of reaction calorimetry and nonlinear state observers for estimation of the states of a chemical process. In order to do that, two distinct chemical reactions will be considered: a) a hydrolysis of acetic anhydride reaction, b) an emulsion copolymerization reaction. The results showed that this approach shows a strong dependence of the tuning parameters, preventing its use for online monitoring of a chemical process. On the other hand, applying the heat balance it is possible to infer continuously the heat release rate and the states of polymerization reactions.

A crescente demanda por produtos poliméricos com propriedades cada vez mais estritas tem forçado o desenvolvimento de técnicas de monitoramento em linha cada vez mais precisas e robustas. Infelizmente, grande parte das principais propriedades poliméricas não são quantificáveis em linha a partir das metodologias analíticas atualmente disponíveis e, portanto, na prática, as propriedades finais dos látices poliméricos são obtidas através da caracterização off line de amostras discretas coletadas do processo, resultando em um tempo de análise longo e indesejado para qualquer algoritmo de controle em tempo real. Por outro lado, como as reações de polimerização são altamente exotérmicas é possível quantificar continuamente a taxa de calor gerado pela reação a partir das medidas de temperatura e do balanço de energia que, por sua vez, pode ser usada para obter importantes informações acerca do estado do processo. Entretanto, esta técnica requer a atualização contínua do coeficiente global de troca térmica ao longo da reação, uma vez que este parâmetro está sujeito a variações temporais significativas. Portanto, o presente trabalho tem por objetivo analisar a viabilidade da aplicação conjunta dos conceitos da calorimetria e dos observadores não-lineares para a estimação dos estados de um processo químico. Para isso, serão analisadas duas reações químicas distintas: a) uma reação de hidrólise de anidrido acético, b) uma reação copolimerização em emulsão. Os resultados obtidos mostraram que essa metodologia é extremamente dependente dos parâmetros de sintonia do observador de estado, inviabilizando o seu uso para o monitoramento em linha de um processo químico. Por outro lado, a aplicação direta do balanço de energia para estimação do calor gerado pela reação, mostrou-se uma forma alternativa simples e viável para a estimação em tempo real dos estados de uma reação de polimerização. / The increasing demand for the production of polymers with more tight properties has placed great emphasis on the development of accurate and robust online monitoring techniques of polymerization reactions. Unfortunately, most of the main characteristics are not measurable online from analytical methodologies currently available and, therefore, in practice, the final properties of polymer latexes are obtained through off line characterization of discrete samples collected from the process, resulting in measurement delay which is undesirable for real-time control. On the other hand, since most of the polymerization reactions are highly exothermic, it is possible to quantify continuously the heat release rate based on temperature measurements and energy balance equations that, in turn, can be used to infer valuable information about the state of process. However, this approach requires up-dating the value of the global heat exchange coefficient through reaction, once this parameter is subject to significant time variations. Therefore, this work aims to examine the feasibility of joint implementation of the concepts of reaction calorimetry and nonlinear state observers for estimation of the states of a chemical process. In order to do that, two distinct chemical reactions will be considered: a) a hydrolysis of acetic anhydride reaction, b) an emulsion copolymerization reaction. The results showed that this approach shows a strong dependence of the tuning parameters, preventing its use for online monitoring of a chemical process. On the other hand, applying the heat balance it is possible to infer continuously the heat release rate and the states of polymerization reactions.

Neste trabalho são apresentadas estratégias para a estimação, em processos químicos, de estados, parâmetros e covariâncias do ruído de processo e das medidas que são testadas com dados experimentais. Para a estimação de estados e parâmetros foram implementadas desde a técnica mais tradicional, o filtro estendido de Kalman (EKF) até as mais modernas da literatura, como o filtro de Kalman Unscented (UKF) e o Moving Horizon Estimator (MHE). A técnica Autocovariance Least-Squares (ALS) permite a estimação das matrizes de covariância do processo e das medidas a partir dos estados medidos dos processos analisados. Três processos foram analisados com as técnicas citadas: a reação de hidrólise de anidrido acético, o aquecimento de um reator de polimerização completamente carregado (sem iniciador) e por fim oito reações diferentes de polimerização em emulsão. Os resultados mostraram que uma sintonia por tentativa e erro para as matrizes de covariância não apresenta um desempenho adequado. Adicionalmente, o UKF mostra um melhor desempenho, quando comparado com o EKF para o monitoramento de processos de polimerização regime em batelada com covariâncias obtidas através de otimização direta. Quando a estimação da covariância com a técnica ALS é implementada e os resultados utilizados em estimadores estocásticos, o desempenho dos estimadores recursivos melhora consideravelmente. Além disso, o MHE mostrou ser uma ferramenta robusta para o monitoramento do coeficiente global de troca térmica (UA) e do calor gerado pela reação para a polimerização em emulsão em regime semi-contínuo. Finalmente, duas características vantajosas da metodologia proposta devem ser destacadas: a independência em relação ao valor inicial para o estado UA e o fato de um único conjunto de matrizes de covariância (quando obtida pela técnica ALS) poder ser utilizado em reações diferentes, sem necessidade de sintonizar novamente as matrizes para cada reação. / In this work, strategies for state, parameter and covariance estimation in chemical processes are presented and tested with experimental data. For state and parameter estimation techniques have been implemented that spread from the traditional Extended Kalman Filter (EKF) to the most modern techniques from literature, such as the Unscented Kalman Filter (UKF) and the Moving Horizon Estimator (MHE). The Autocovariance Least-Squares technique (ALS) allows the covariance matrices of the process and measurement noise to be estimated based on the measured states of the processes analyzed. Three cases were studied using these techniques: the hydrolysis of acetic anhydride, the warming-up stage of a fully charged polymerization reactor (without initiator) to the desired temperature and finally, eight different emulsion polymerization reaction runs. Results showed that determining covariance matrices by trial and error does not lead to an adequate performance. Additionally, the UKF presents a better performance than the EKF for batch polymerization processes with covariance matrices obtained by direct optimization. When the estimation of the covariance is performed by the ALS technique and they are used in a stochastic estimator, the performance of the recursive estimators is considerably improved. Furthermore, the MHE proved to be a robust tool for monitoring the overall heat transfer coefficient (UA) and the heat of reaction for fedbatch emulsion polymerization. Finally, two positive features of the proposed methodology must be highlighted, its low dependency on the initial state condition of UA and the fact that a unique set of covariance matrices (when obtained by the ALS technique) can be used for different reaction runs, without the necessity of tuning the matrices again for each reaction.

Recent studies have shown that general-base assisted catalysis is a viable mechanistic pathway for hydrolysis of smaller anhydrides. Therefore, it is the central purpose of the present work to compare and contrast the number of hydrogen atoms in-flight and stationary in the transition state structure of the base-catalyzed mechanisms of 2 hydrolytic reactions as well as determine if any solvent effects occur on the mechanisms. The present research focuses on the hydrolytic mechanisms of N,N-dimethylformamide (DMF) and acetic anhydride in alkali media of varying deuterium oxide mole fractions. Acetic anhydride has been included in this study to enable comparisons with DMF hydrolysis. Comparative studies may give synergistic insight into the detailed structural features of the activated complexes for both systems. Hydrolysis reactions in varying deuterium oxide mole fractions were conducted in concentrations of 2.0M, 2.5M, and 3.0M for DMF and 0.10M for acetic anhydride at 25°C. Studies in varying deuterium mole fractions allow for proton inventory analysis, which sheds light on the number and types of hydrogen atoms involved in the activated complex. For these systems, this type of study can distinguish between direct nucleophilic attack of the hydroxide ion on the carbonyl center and general-base catalysis by the hydroxide ion to facilitate a water molecule attacking the carbonyl center. The numerical data are used to discuss 3 possible mechanisms in the hydrolysis of DMF.

The thesis entitled “Chemistry of Tetrathiomolybdate: Applications in Organic Synthesis” is divided in to six chapters Chapter 1: Synthesis of -amino disulfides, cystines and their direct incorporation into peptides mediated by tetrathiomolybdate In this chapter, we report a simple method for direct access to β-amino disulfides by regioselective ring opening of sulfamidates with benzyltriethylammonium tetrathiomolybdate [BnEt3N]2MoS4. The versatility of this reaction has been shown by preparing a number of β-amino disulfides having different N-protecting groups and the stability of these protecting groups under the reaction conditions has been evaluated. This methodology is also extended to the synthesis and direct incorporation cystine and 3, 3′-dimethyl cystine derivatives into peptides. Chapter 2: Unusual reactivity of tetrathiomolybdate: A new entry to the synthesis of b-aminothiols In this chapter, we disclose a simple and highly efficient method for the synthesis of β and γ-amino thiols via regioselective ring opening of sulfamidates with tetrathiomolybdate 1. The scope and generality of this methodology has been exemplified by synthesizing a carbohydrate derived β-aminothiol. This methodology has also been extended to the synthesis of isocysteine derivatives in optically pure form. Chapter 3: Part 1: Synthesis of β-aminodiselenides via sequential one-pot, multistep reactions mediated by tetrathiomolybdate In this chapter, we have demonstrated that a variety of N-alkyl-β-aminodiselenides can be synthesized in high yield from appropriate sulfamidates under mild reaction conditions using potassium selenocyanate and tetrathiomolybdate [BnEt3N]2MoS4 via a sequential one-pot multistep process. The compatibility of different protecting groups under the reaction conditions has been discussed. Chapter: 3 Part 2: Synthesis of unnatural seleno amino acids and their direct incorporation into peptides In this chapter, we have demonstrated the first and general method for the synthesis of selenocystine, 3, 3'-dialkylselenocystine, isoselenocystine and their direct incorporation into peptides using a one-pot multistep reaction strategy mediated by tetrathiomolybdate. Chapter 4: Synthesis and functionalization of cysteine, selenocysteine and their derivatives via the formation of unsymmetrical disulfide and sulfur-selenium bond. In this chapter, we present a novel one-pot multi component strategy for the synthesis and functionalization of cysteine, selenocysteine and their derivatives via unsymmetrical disulfides and sulfur-selenium bond formation. Chapter 5: Part 1: A novel method for the synthesis of thioacetates employing benzyltriethylammonium tetrathiomolybdate and acetic anhydride In this chapter, we report a simple and efficient methodology for the synthesis of thioacetates using benzyltriethylammonium tetrathiomolybdate [BnEt3N]2MoS4 and acetic anhydride as the key reagents, starting from alkyl halides in a multi step, tandem reaction process. The application of this methodology for the synthesis of orthogonally protected cysteine derivatives and anomeric β-thioglycosides has also been demonstrated. Chapter 5: Part 2: One-pot synthesis of β-aminothioacetates using benzyltriethyl-ammonium tetrathiomolybdate and acetic anhydride. In this chapter, we have demonstrated a simple and efficient method for the synthesis of β-amino thioacetates and pseudo thioinositol derivatives, via ring opening of aziridines and aziridino epoxides using tetrathiomolybdate 1 and acetic anhydride as key reagents. Chapter 6: Simple and efficient synthesis of allo and threo-3, 3'-dimethylcystine derivatives in optically pure form In this chapter, we have presented a simple and efficient methodology for the synthesis of allo-3,3'-dimethylcystine and threo-3,3'-dimethylcystine derivatives in optically pure form using L-threonine as the chiral pool and benzyltriethylammonium tetrathiomolybdate 1 as the key reagent. (For structural formula pl see the pdf file)