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Some thermochemical studies on aliphatic nitrilesIwanciow, Bernard Louis, January 1950 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1950. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 124-125).
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De Ramanspectra van cen aantal alifatische polychloorverbindingen ...Rijnders, George Wilhelm August. January 1900 (has links)
Proefschrift--Amsterdam. / "Litteratuurlijst": p.[110]-111.
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De Ramanspectra van cen aantal alifatische polychloorverbindingen ...Rijnders, George Wilhelm August. January 1900 (has links)
Proefschrift--Amsterdam. / "Litteratuurlijst": p.[110]-111.
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The kinetics of catalytic vapor-phase esterification of some aliphatic alcoholsHeath, Carl Ernest, January 1956 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1956. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 140-143).
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The evaluation of autoxidation procedures for the selective oxidation of aliphatic alcoholsBacela, Siyabulela Mawande January 2001 (has links)
The homogeneously catalyzed oxidation of 1-propanol by dioxygen in glacial acetic acid using cobalt(II)acetate and sodium bromide as the catalyst system has been investigated with the view of determining the significance of various experimental variables during the oxidation. The results of this investigation show unequivocally that a number of reaction variables have a direct influence upon catalytic activity and hence the reaction products. It is quite evident that the major product of this autoxidation reaction is propionic acid with the respective esters as side-products. This is an indication that the autoxidation mechanism occurs via a two-stage pathway, namely, the oxidation of 1-propanol to propionaldehyde as the primary product and, subsequently, the further oxidation of the propionaldehyde to propionic acid as the major product. Thus the esterification process of the propionic acid with the substrate 1-propanol could be termed as a side-reaction because its not facilitated by the catalyst system and it consumes the formed product. The catalyst activity has been demonstrated to depend on a number of factors, including the bromide concentration, the cobalt(II)acetate concentration, the water concentration, reaction temperature, and the presence of metal acetates as co-catalysts. There is an observed decrease in catalytic activity at high bromide concentration, which may be explained in terms of cobalt bromide complexes that form at these high concentrations. Subsequently, the same trend of catalyst activity reduction at high cobalt(II)acetate concentration may be ascribed to the “inactive” metal complexes that are susceptible to form at high metal ion concentrations. The catalytic activity increases with increase in total concentration and rapidly decreases at very high concentrations. This can be explained in terms of the observations made during the investigation of the effect of cobalt(II)acetate and bromide concentrations. The high increase in catalytic activity with increasing temperature is ascribed to the Arrhenius law, which relates the rate constant for a particular reaction to temperature. However, there is an observed loss of catalyst selectivity at high temperatures which maybe due to two possible factors. The first is simply related to an increased loss of volatile material from the reactor in the oxygen gas stream as the temperature is increased. The second relates to the increasing activity of the catalyst system for the selective decarboxylation of the carboxylic acid product. The addition of water to the reaction system rapidly reduces the catalyst activity. This detrimental effect is an indication that there is an effective competition by water with bromide for coordination sites on cobalt(II), thereby preventing the formation of the active catalyst species. The introduction of metal acetates as co-catalyst reduces the catalyst activity quite dramatically. This inhibition effect is suggested to relate to the redox potential of the respective metal ions. The results of statistical analysis of the experimentally derived response surface during the oxidation of 1-propanol, show no significant lack of fit, and the residuals obtained by applying the response surface to the design settings show that the data is normally distributed. The response surface is therefore reliable, but keeping in mind that the central composite design used is not rotatable so that its predictive power, especially outside the experimental domain investigated, is quite limited. However, several interesting observations were still possible The oxidative dehydrogenation of ethanol over supported noble-metal catalysts has been investigated with the view of identifying the most active supported noble-metal and also to compare this oxidation procedure with the autoxidation procedure. Secondly, the effect of an acidic resin as a co-catalyst was also investigated during the said oxidation. On the basis of results presented in this study during oxidative dehydrogenation of ethanol, catalysts no.2 (10% Pd/C), 8 (2% Pd/Al – Pb-promoted) and 9 (2% Pt/8% Pd/C) appear to be the most active in terms of relative rates, while catalysts 6 (10% Pd/C- Pbpromoted), 7 (5% Pd/C-shell reduced-Pb -promoted) and 10 (5% Pt 5% Pd on C) are more active based on the comparison of average rates. Two other observations are of interest. Firstly, the promotion of the Pd catalysts with lead appears to improve catalyst activity to some extent as shown by the comparisons between catalysts 1 and 5, 4 and 8, 2 and 6 and 3 and 7. Secondly, the introduction of Pt up to equal amounts with palladium seems to produce the most active catalysts. On its own, platinum appears to be a better catalyst than Pd when supported on activated carbon (catalysts 1 and 12). In comparison with the homogeneous, cobalt-bromide catalyzed oxidation of 1- propanol in the liquid-phase, oxidations over noble-metal catalysts in the liquid-phase appear to be significantly less active. The presence of the resin promoted the formation of ethyl acetate to some extent, the improvements are not as dramatic as expected.
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Synthesis of highly branched aliphatic compounds /Arkell, Alfred January 1958 (has links)
No description available.
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Syntheses and properties of highly sterically hindered aliphatic compounds /Fukunaga, Tadamichi January 1959 (has links)
No description available.
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Part I: The endecaphyllins: naturally occuring aliphatic nitro-compounds. Part II: Mammeigin: a new naturally occuring 4-phenyl coumarin /Mueller, Wolfgang Heinz January 1964 (has links)
No description available.
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Aerobic cometabolism of chlorinated aliphatic hydrocarbons by a butane-grown mixed culture : transformation abilities, kinetics and inhibitionKim, Young 22 February 2000 (has links)
Graduation date: 2000
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Calorimetric investigations of the self-association of aliphatic carboxylic acids in organic solventsZaugg, Noel S. 01 August 1975 (has links)
A calorimetric enthalpy of dilution technique was applied to the investigation of carboxylic acid self-association in organic solvents at 25°C. Data were analyzed in terms of the apparent relative molar enthalpy, Φ_L, and were found to fit adequately a monomer-dimer model. Values of the thermodynamic dimerization parameters K_2 and ΔH°_2 were obtained for several methyl-, halo-, and phenyl-substituted acetic and propionic acids in benzene. Some of the acids were also studied in toluene and carbon tetrachloride. Substituent effects on K_2 and ΔH°_2 were in general small and were explained adequately by an electrostatic model of the monomer-dimer interaction. Solvent effects were explained by considering an acid-solvent interaction. The effect on the results of small amounts of water in the solvent was found to be a function of aqueous acid strength. Acetic acid and other weak acids were unaffected by water in the solvent, but a significant affect was observed with stronger acids, such as the haloacetic acids.
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