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Thesis (Ph. D.)--Institute of Paper Chemistry, 1965. / Includes bibliographical references (p. 116-119).

Thesis (Ph. D.)--University of Wisconsin--Madison, 1937. / Typescript. Includes abstract and vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references.

The following thesis outlines work carried out during the last three years for the development and investigation of methodologies using amides as N- and O- acylating agents. Chapter 1 highlights the range of methodologies and protocols reported in the literature that use amides as precursors for the synthesis of both functionalised amides and esters. The introduction will highlight the range of catalysts and promoters used as well as the scope of the current methodologies. As well as this it will highlight the limitations of the methodologies so emphasising where the following research fits into these areas. Chapter 2 presents the development of a transamidation methodology using zirconocene dichloride as a catalyst. The scope with respect to functional group tolerance is presented as well as the investigations into the mechanism of the reaction. Chapter 3 builds on the research presented in Chapter 2 and details the development of a more catalytically active zirconocene transamidation methodology. By the addition of a catalytic additive the temperature or time required for the reaction to be carried out could be lowered. Investigations into the mechanism were also carried out highlighting the in situ formation of an active catalytic species. Chapter 4 details the development of an operationally simple methodology for the O-acylation of alcohols using amides. Using a catalytic amount scandium triflate the substrate scope of the reaction was explored with a proposed mechanism presented based on activation of the amide.

Thesis (Ph. D.)--Institute of Paper Chemistry, 1974. / Includes bibliographical references (leaves 81-84).

Thesis (Ph. D.)--Institute of Paper Chemistry, 1955. / Bibliography: leaves 106-109.

Water has long been assumed to be essential for biological function. To understand the molecular basis of the role of water in protein function, several studies have established a correlation between enzyme activity and hydration level. While a threshold of hydration of 0.2 h (grams of water per gram of dried protein) is usually accepted for the onset of enzyme activity, recent works show that enzyme activity is possible at water contents as low as 0.03 h (Lind et al., 2004). Diffusion limitation in these experiments was avoided by monitoring enzyme-catalyzed hydrolysis of gas-phase esters. However, since water is also a substrate for the enzyme used in these experiments, they cannot be used to probe the possibility of activity at zero hydration. However, the pig liver esterase and C. rugosa lipase B are able to catalyse alcoholysis reactions in which an acyl group is transferred between an ester and an alcohol. Therefore, by following this reaction and using a gas phase catalytic system, we have been able to show that activity can occur at 0 g/g. These results led to the question of the accuracy of determinations of very low water concentrations; i.e., how dry is 0 g/g? Although gravimetric measurements of the hydration level do not allow us to define the anhydrous state of the protein with sufficient sensitivity, using 18O-labeled water, we have been able to quantify the small number of water molecules bound to the protein after drying, using a modification of the method of Dolman et al. (1997). Testing different drying methods, we have been able to determine a level of hydration as low as 2 moles of water per mole of protein (equivalent to 0.0006 h in the case of pig liver esterase) and have shown that in the case of the pig liver esterase, activity can occur at this hydration level. At the molecular level, if the hydration level affects activity, we can expect an effect on the protein dynamics. Neutron scattering spectra of hydrated powders, for instance, show that diffusive motions of the protein increase with the hydration (Kurkal et al., 2005) To address the question of the protein motions involved in the onset of enzyme activity at low hydration, we performed neutron scattering experiments on a pico-second time scale on dried powders. Preliminary results show a dynamical transition at hydration levels as low as 3 h. Molecular dynamic simulations have also been used in this study to access the dynamics of the active site. Overall, the results here show that pig liver esterase can function at zero hydration, or as close to zero hydration as current methods allow us to determine. Since the experimental methodology restricts this work to a small number of enzymes, it is unlikely that it will ever be possible to determine if all enzymes can function in the anhydrous state: however, the results here indicate that water is not an obligatory requirement for enzyme function.

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Neste estudo foi investigada a alcoólise enzimática do óleo de soja com etanol, utilizando t-butanol como solvente e enzimas imobilizadas Lipozyme TL IM, Lipozyme RM IM e Novozym 435 como catalisadores. As reações foram realizadas em um reator batelada fechado acoplado a um condensador e com constante agitação. Foram avaliadas a influência do t-butanol, do tipo de enzima utilizada, da razão molar álcool/óleo e da temperatura no rendimento em biodiesel. A etanólise do óleo de soja por sucessivas adições de álcool foi investigada e as melhores condições foram obtidas em presença de t-butanol, razão molar etanol/óleo igual a 3, temperatura de 50C e 5% (m/m) de Novozym 435. Nas reações conduzidas em presença de t-butanol não foram observadas diferenças significativas entre a adição direta e a escalonada do álcool. Os efeitos da adição de álcool só foram observados na ausência de t-butanol. O rendimento máximo em ésteres etílicos atingido foi cerca de 66% após 4h de reação com Novozym 435 na presença de solvente. / In this research, the enzymatic alcoholysis of soybean oil was investigated by using commercial immobilized lipases: Lipozyme TL IM, Lipozyme RM IM and Novozym 435 as catalysts. The reactions were carried out in a closed batch reactor with constant stirring and coupled with condenser. The influence of t-butanol, type of enzyme, molar ratio (alcohol/soybean oil) and temperature on biodiesel yield were evaluated. The ethanolysis of soybean oil by stepwise additions of ethanol was also investigated. The best conditions were obtained in t-butanol presence with ethanol/oil molar ratio of 3, temperature of 50oC and 5 wt.% Novozym 435. For the reactions carried out with t-butanol, the effects of stepwise alcohol addition were not observed, but it was realized in t-butanol absence. The maximum biodiesel yield achieved was 66% after 4h of reaction with Novozym 435 in t-butanol system.

Neste trabalho, foi investigada a alcoólise do óleo de soja com álcool utilizando uma lipase comercial imobilizada (Lipozyme RM IM). As reações foram realizadas em um reator batelada fechado acoplado a um condensador e com constante agitação. Foi determinada a influência do álcool (metanol ou etanol), quantidade de enzima, razão molar álcool/óleo de soja, solvente e temperatura na produção de biodiesel. A etanólise do óleo de soja por sucessivas adições de álcool foi investigada. As melhores condições foram obtidas em um sistema livre de solvente com razão molar etanol/óleo igual a 3,0, temperatura de 50C e concentração de enzima de 7% em massa. A etanólise em batelada com 3 adições sucessivas foi a mais eficiente para a produção de biodiesel. Nessas condições, o rendimento em ésteres etílicos foi cerca de 55% após 2h de reação. A alcoólise de óleo de soja com metanol e etanol também foi estudada com KOH. O efeito do álcool (metanol ou etanol), concentração do catalisador e razão molar entre álcool e óleo de soja foi determinada. O maior rendimento (92%) na alcoólise do óleo de soja com KOH foi obtido com metanol / In this work, enzymatic alcoholysis of soybean oil with alcohol was investigated using a commercial immobilized lipase (Lipozyme RM IM). Reactions were carried out in a closed batch reactor with constant stirring and coupled with condenser. The influence of alcohol (methanol or ethanol), enzyme amount, molar ratio of alcohol to soybean oil, solvent (n-hexane) and temperature on biodiesel production was determined. The ethanolysis of soybean oil by successive additions of ethanol was also investigated. The best conditions were obtained in a solvent-free system with ethanol/oil molar ratio of 3.0, temperature of 50oC and enzyme concentration of 7.0% (w/w). Three-step batch ethanolysis was most effective for the production of biodiesel. In these conditions, ethyl esters yield was about 55% after 2 hours of reaction. Alcoholysis of soybean oil with methanol and ethanol were also investigated using KOH. The effects of alcohol (methanol or ethanol), catalyst concentration and molar ratio of alcohol to soybean oil was determined. The highest yield (92%) in the alcoholysis of soybean oil using KOH was obtained with methanol