Thesis (Ph. D.)--University of Missouri-Columbia, 1997. / Typescript. Vita. Includes bibliographical references (leaves 173-179). Also available on the Internet.

Thesis (Ph. D.)--University of Missouri-Columbia, 1997. / Typescript. Vita. Includes bibliographical references (leaves 173-179). Also available on the Internet.

Thesis (M.S.)--University of California, Santa Cruz, 1992. / Typescript. Includes bibliographical references (leaves 48-51).

Fatigue tests on compact tension specimens of 90-10 copper nickel were conducted in 3.5% NaCl solutions. Anodic or cathodic currents were applied during testing. Anodic currents decreased and cathodic currents increased the fatigue life. Both anodic and cathodic currents changed the fracture mode from predominantly transgranular to intergranular. Constant extension rate tests were performed on similar CT specimens in environments of 3.5% NaCl solution and 3.5% NaCl solution titrated to pH 1.0 with various levels of applied current. The environment had little influence on the monotonic failure of 90-10 copper nickel. Polarization studies were conducted to determine the effects of welding and pH on the corrosion behavior of 90-10 copper nickel. The rate of corrosion was less in the weld and the heat affected zone than in the base metal. As the pH of the environment was lowered, the corrosion rate of 90-10 copper nickel increased due to the retardation of film formation and repassivation. These studies showed that three different mechanisms of corrosion fatigue were likely: localized anodic dissolution, surface film rupture and hydrogen embrittlement. The dominance of one mechanism over the other two depends on the applied current. No evidence of susceptibility to stress corrosion cracking was found, therefore, a true corrosion fatigue process is operative in 90-10 copper nickel. / Master of Science / incomplete_metadata

No description available.

Discovery of mesoporous materials by Mobil researchers in 1992 opened a new field in catalytic applications. The materials designated as M41S family are MCM-41 with one-dimensional hexagonal structure, MCM-48 with three-dimensional cubic structure and MCM-51 with unstable lamellar structure. This family of materials have high surface areas up to 1500 m2/g, narrow pore size distributions with pore sizes varying from 20 to 100 &Aring / . These materials can be activated by incorporation of metals or active compounds into their structures. In this study, copper and nickel incorporated MCM-41 type catalytic materials were synthesized via different methods namely, impregnation, high temperature and low temperature direct synthesis methods. The Cu-MCM-41, and Ni-MCM-41, as well as synthesized MCM-41 were characterized by using XRD, TEM, N2 sorption, SEM, XRF, EDS, AAS and TPR. MCM-41 was synthesized with high temperature direct synthesis method. High surface area values up to 1400 m2/g of MCM-41 mesoporous materials were obtained with high pore volumes up to 1.17 cc/g. Cu-MCM-41 type catalytic materials were synthesized with three different methods. Impregnation and high temperature direct synthesis methods gave better results than those of low temperature direct synthesis method. In impregnation, relatively high surface area values (730 m2/g) were obtained with Cu/Si mole ratio as high as 0.3 in the product. For the case of high temperature direct synthesis products, Cu/Si mole ratios as high as 0.26 were obtained with somewhat smaller surface areas (400 m2/g). Low temperature direct synthesis method is the least favorable method in metal loading. Ni-MCM-41 type of catalytic materials were synthesized by impregnation and high temperature direct syntheses methods. Ni incorporation by high temperature direct synthesis method gave high surface area values (560-930 m2/g) having Ni/Si mole ratios of 0.12-0.28.

Heavy metals are well known toxic priority pollutants. Hence, wastewaters containing these species must be treated prior to discharge into receiving bodies. In this study, the potential of Bigadi&ccedil / clinoptilolite for Cu2+ and Ni2+ removal from wastewaters was investigated in batch and continuous reactors. Results of the preliminary experiments revealed the optimum operating conditions, namely, initial solution pH of 5 and 4 for Cu2+ and Ni2+, respectively and contact time of 48 hours. Additionally, conditioning of clinoptilolite with 2M NaCl solution for 24 hours was found to considerably improve the capacity utilized at breakthrough. Maximum removal capacities and prevailing mechanisms in the system were investigated via equilibrium studies under preliminary determined optimum operating conditions. Langmuir and Freundlich models were fitted to the experimental data and Langmuir model was found to be better in describing the system behavior. Maximum removal capacities obtained from non-linear regression of Langmuir model are almost the same for Cu2+ and Ni2+ removal using as received clinoptilolite samples (0.31 and 0.32 meq/g respectively). However, conditioned clinoptilolite samples exhibit higher capacity for Cu2+ over Ni2+ (0.5 and 0.43 meq/g, respectively). Analyses of exchangeable cations in the aqueous phase were carried out to examine the prevailing mechanisms in the system. As a result, adsorption, dissolution of clinoptilolite and surface precipitation (particularly in the case of Cu2+ removal) are considered to accompany ion exchange. Finally, fixed-bed column studies were conducted with conditioned clinoptilolite samples for Cu2+ removal. An improvement in Cu2+ uptake was observed with decreasing volumetric flow rate (from 8 BV/h to 2-4 BV/h) and decreasing particle size (from 1.180-1.400 mm to 0.833-1.180 mm). Analyses of exchangeable cations as well as Si4+, Fe(total) and Al3+ were also carried out to examine the prevailing mechanisms. Ion exchange was discussed as the predominant mechanism in the system with minor contributions from adsorption and dissolution of clinoptilolite to the total amount of Cu2+ uptake and to the total amount of exchangeable cations release, respectively.

Thesis (M.S.)--University of California, Santa Cruz, 2001. / Typescript. Includes bibliographical references (leaves 69-72).

Thesis (Ph. D.)--Ohio State University, 2005. / Available online via OhioLINK's ETD Center; full text release delayed at author's request until 2006 Nov 29

FundaÃÃo Cearense de Apoio ao Desenvolvimento Cientifico e TecnolÃgico / Bodies of water contamination problems have stimulated many researchers around the world in the search for alternatives to solve or minimize the effects caused by discharges of toxic materials to the environment. What is desired, preferably, is that such solutions are economically viable and efficient. Toxic metals on the list of the main contaminants of water bodies. Because these are very dangerous chemicals, this class of materials has led many research groups seeking to achieve avoid contamination of water bodies by this type of material. The wastewater generated by electroplating industries have a high concentration of metal ions, so it should be treated before discharge to receiving waters. The processes using adsorption emerge as one of the research lines most valued by many researchers in order to contribute to this issue. Electrochemical processes have also been tested in the remediation of wastewater contaminated with various pollutants, including toxic metals. Natural clays play an important role in this type of study. Several studies have shown very promising results with the use of such material in the removal of toxic metals. This paper aims to conduct a comparative study of removal efficiency of Cu (II), Ni (II), Cd (II) and Pb (II) from six natural clays Brazilian soil. The clays were used: sodium Clay (AS), green clay (AV), clay chocolate calcium (ACCA), ferric clay (AF), attapulgite (AT) and kaolin (CAU). Balance studies were performed through adsorption isotherms in batch systems. For the balance of studies used monoelementares systems and multielement containing the four metal ions. We have also performed the kinetic study to evaluate the lower equilibrium times. Finally experiments were conducted with hybrid systems which use electrocoagulation-adsorption and coagulation with the purpose of working in a continuous system. The results show that all clays have good adsorption capacity for the four ions. The adsorption equilibrium results were compared with the Langmuir, Freundlich and Temkin. The maximum adsorption capacity obtained from monoelementares solutions were: 50.76 mg.g-1 [AS / Pb (II)], 50.76 mg.g-1 [AV / Cu (II)], 57.14 mg.g-1 [ACCA / Cu (II)], 34.72 mg.g-1 [AF / Cu (II)], 169.4 mg.g-1 [AT / Pb (II)] and 10 29 mg.g-1 [CAU / Cu (II)]. The kinetic model best suited to the experimental data was the pseudo second order. The Webber-Morri diffusion models and Boyd show that adsorption processes occur in more than one step and that in the early days predominates intrafilme diffusion process. The electrocoagulation-clotting experiments associated with adsorption with clays are promising because it promoted an increase in the removal capacity and facilitate the separation of the clay from the aqueous phase. The ion removal capacities of Cu (II) from industrial wastewater using the hybrid system were: 54% [AL / AS] to 45% [Al / ACCA] to 57% [Al / HF] 33% to [AL / AT], 48% / Problemas de contaminaÃÃo dos corpos hÃdricos tÃm estimulado muitos pesquisadores em todo mundo na busca de alternativas que resolvam ou minimizem os efeitos causados pelos descartes de materiais tÃxicos ao meio ambiente. O que se deseja, preferencialmente, à que tais soluÃÃes sejam economicamente viÃveis e eficientes. Os metais tÃxicos fazem parte da lista dos principais contaminantes dos corpos hÃdricos. Por se tratarem de substÃncias quÃmicas bastante perigosas, esta classe de material tem levado muitos grupos de pesquisa na busca de conseguir evitar a contaminaÃÃo dos corpos hÃdricos por este tipo de material. Os efluentes gerados pelas indÃstrias de galvanoplastia possuem uma elevada concentraÃÃo de Ãons metÃlicos, por isso devem ser tratados antes do descarte aos corpos receptores. Os processos que usam adsorÃÃo despontam como uma das linhas de pesquisas mais avaliadas por inÃmeros pesquisadores no intuito de contribuir com esta problemÃtica. Os processos eletroquÃmicos tambÃm tÃm sido testados na remediaÃÃo de efluentes contaminado por diversos poluentes, inclusive metais tÃxicos. As argilas naturais desempenham um papel importante neste tipo de estudo. Diversos trabalhos vÃm apresentando resultados bastante promissores com o uso deste tipo de material na remoÃÃo de metais tÃxicos. Este trabalho se propÃe a realizar um estudo comparativo de eficiÃncia de remoÃÃo dos Ãons Cu(II), Ni(II), Cd(II) e Pb(II) a partir de seis argilas naturais de solo brasileiro. As argilas utilizadas foram: Argila sÃdica (AS), argila verde (AV), argila chocolate cÃlcica (ACCA), argila fÃrrica (AF), atapulgita (AT) e caulim (CAU). Foram realizados estudos de equilÃbrio atravÃs de isotermas de adsorÃÃo em sistemas de batelada. Para os estudos de equilÃbrio utilizaram-se sistemas monoelementares e multielementares contendo os quatro Ãons metÃlicos. Realizou-se tambÃm o estudo cinÃtico para avaliarmos os menores tempos de equilÃbrio. Por fim foram realizados experimentos com sistemas hÃbridos que utilizam adsorÃÃo e eletroflotaÃÃo-coagulaÃÃo, com a finalidade de trabalharmos em sistemas contÃnuos. Os resultados obtidos mostram que todas as argilas apresentam boa capacidade de adsorÃÃo para os quatro Ãons. Os resultados de equilÃbrio de adsorÃÃo foram confrontados com os modelos de Langmuir, Freundlich e Temkin. As capacidades mÃximas de adsorÃÃo obtidas a partir de soluÃÃes monoelementares foram: 50,76 mg.g-1 [AS/Pb(II)], 50,76 mg.g-1 [AV/Cu(II)], 57,14 mg.g-1 [ACCA/ Cu(II)], 34,72 mg.g-1 [AF/ Cu(II)], 169,4 mg.g-1 [AT/Pb(II)] e 10,29 mg.g-1 [CAU/Cu(II)]. O modelo cinÃtico que melhor se adequou aos dados experimentais foi o de pseudo segunda ordem. Os modelos de difusÃo de Webber-Morri e Boyd demonstram que os processos de adsorÃÃo ocorrem em mais de uma etapa e que nos primeiros tempos predomina o processo de difusÃo intrafilme. Os experimentos de eletroflotaÃÃo-coagulaÃÃo associados à adsorÃÃo com argilas mostraram-se promissores porque promoveram um incremento nas capacidades de remoÃÃo e facilitam a separaÃÃo dos argilominerais da fase aquosa. As capacidades de remoÃÃo do Ãon Cu(II) a partir do efluente industrial usando o sistema hÃbrido foram: 54% para [AL/AS], 45% para [AL/ACCA], 57% para [AL/AF] 33% para [AL/AT], 48% para [FE/AS], 47% para [FE/ACCA], 54% para [FE/AF] e 40% para [FE/AT].