No description available.

No description available.

No description available.

No description available.

Pinhole leaks in copper plumbing pipes are a big concern for the homeowners. The problem is spread across the nation and remains a threat to plumbing systems of all ages. Due to the absence of a single acceptable mechanistic theory no preventive measure is available to date. Most of the present mechanistic theories are based on analysis of failed pipe samples however an objective comparison with other pipes that did not fail is seldom made. The variability in hydraulic and water quality parameters has made the problem complex and unquantifiable in terms of plumbing susceptibility to pinhole leaks. The present work determines the spatial and temporal spread of pinhole leaks across United States. The hotspot communities are identified based on repair histories and surveys. An assessment of variability in water quality is presented based on nationwide water quality data. A synthesis of causal factors is presented and a scoring system for copper pitting is developed using goal programming. A probabilistic model is presented to evaluate optimal replacement time for plumbing systems. Methodologies for mechanistic modeling based on corrosion thermodynamics and kinetics are presented. / Master of Science

Nos últimos anos houve, no Brasil, um significativo investimento em usinas de álcool para suprir a demanda. Todavia, surgiram problemas de natureza econômica e ambiental, já que a tecnologia atualmente utilizada nas destilarias de álcool produz em média 13 litros de vinhaça para cada litro de álcool. Na busca de uma solução para reduzir o volume deste resíduo, desenvolveu-se um equipamento para concentração de vinhaça, denominado Ecovin, pela empresa Citrotec localizada em Araraquara-SP. Para cada Ecovin são utilizados cerca de 4000 tubos com costura nos trocadores de calor, e para reduzir seu custo de fabricação, avaliou-se como opção o uso de tubos da liga AISI 444. Inserido neste contexto, o presente trabalho procurou caracterizar os mecanismos de corrosão e mostrar de forma comparativa o desempenho dos tubos nas juntas tubo-espelho. Estudo-se, portanto, dois tipos de junta, a do projeto atual, composta por chapa e tubo da liga AISI 316L; e a nova proposta, composta por chapa da liga AISI 316L e tubo da liga AISI 444. Para tanto, iniciou-se com a avaliação da soldabilidade das ligas estudadas, através da caracterização microestrutural, qualificação do procedimento de soldagem da junta tubo-espelho e de ensaios de sensitização nas soldas. Em seguida, ensaios de perda de massa por imersão foram realizados nas soluções de 0,5 M \'H IND.2\'SO IND.4\' e 0,5 M \'H\'CL\', nas temperaturas de 30°C, 50°C, 70°C e 90°C, de acordo com o intervalo de temperatura de operação do Ecovin. Nas mesmas soluções, e na temperatura ambiente, foram realizados ensaios eletroquímicos de polarização potenciodinâmica em amostras que reproduziram o ciclo térmico de soldagem das juntas tubo-espelho estudadas, nas regiões do metal de base, zona afetada pelo calor (ZAC) e no metal de solda. Na junta tubo-espelho a corrosão ocorreu preferencialmente na ZAC formada entre a interface tubo-metal de solda, e no cordão de solda à margem do tubo, com a atuação de mecanismos de corrosão generalizada e localizada. Na junta tubo-espelho dissimilar observou-se que o processo corrosivo foi predominante na superfície do tubo AISI 444, típico do mecanismo de corrosão galvânica, onde o tubo AISI 444 caracterizou-se como a região anódica. O desempenho da liga AISI 316L, assim como a junta soldada composta somente por essa liga, apresentou um melhor desempenho em corrosão, porém, na solução contendo cloreto, a variação da temperatura exerceu uma influência proporcional para ambos os casos avaliados nesse estudo. Destaca-se ainda que a liga AISI 316L sofreu corrosão por pite na ZAC e no metal de solda, em ambas as soluções, com maior severidade do que a liga AISI 444. Os resultados obtidos indicam que para a aplicação requerida, o tubo AISI 444 pode ser utilizado na temperatura de 50°C com satisfatório desempenho e similar à junta composta somente por AISI 316L. / Recently in Brazil there has been constant investments in ethanol plants, to supply the internal and external market, resulting at a high increase of the volume of this product. However, economical and environmental problems arose because of this new demand, whereas the current technologies produce thirteen liters of vinasse for each liter of alcohol. Each ECOVIN uses nearly 4000 welded tubes in the heat exchangers, and there is an option to use welded AISI 444 alloy tubes in order to reduce the manufacture costs of the ECOVIN. In this context, this work determines the corrosion mechanisms and analyzes the performance of welded tubes and the tube-to-tubesheet welded joints. The following types of tube-to-tubesheet were evaluated: current welded joints of this project, with all components manufactured with AISI 316L alloy; and the welded joint suggested for the project, using the welded tubes of AISI 444 alloy and the plate of AISI 316L alloy. For this purpose, the first step was to evaluate the weldability of the studied alloys, through microstructural characterization, welding procedure qualification and the intergranular corrosion test. After that, mass loss tests were conducted in 0,5 M \'H IND.2\'SO IND.4\' and 0,5 M \'H\'CL\' solutions, at 30°C, 50°C, 70°C and 90°C, according to the temperature range of the equipment operating. Electrochemical polarization tests were made in the same solution concentration used in the mass loss tests, but only in room temperature. These tests were made in samples that were welded with the same thermal cycle of the tube-to-tubesheet welded joints, and the evaluations were made on the base metal, heat affected zones and weld metal. The uniform and localized corrosion process occurred preferentially in the interface formed between tube and weld metal, and on weld metal near the tubes. In the tube-to-tubesheet dissimilar welded joints, it was observed that the corrosion process was predominant on the surface of AISI 444 alloy, probably because of the galvanic corrosion process, where the AISI 444 was an anodic region. The best performance on corrosion process was observed in AISI 316L, both the base metal and the similar welded joints. However, for the tests in chloride environment, in this process, the temperature caused a proportional influence in the corrosion rate of AISI 316L and AISI 444. In the AISI 316L alloy it was observed nucleation of pitting in HAZ and in weld metal, in both solutions, and more aggressive than observed in the AISI 444 alloy. The results showed that the AISI 444 alloy can be applied for the initial ranging temperatures of the equipments operation, with satisfactory performance.

Projetos de instalações industriais com requisitos de assepsia e resistência à corrosão têm os aços inoxidáveis austeníticos como materiais de engenharia, e a liga AISI 316L é amplamente utilizada. A soldagem de chapas espessas é executada por processos MIG e a qualificação do procedimento de soldagem é realizada com base em propriedades mecânicas, avaliação insuficiente para aplicações que necessitam de uma película passiva resistente. A microestrutura da zona fundida da liga AISI 316L exerce influência sobre a resistência à corrosão, e há a necessidade de definir os mecanismos que governam a influência da fase sigma na resistência à corrosão. Inserido neste contexto, o objetivo do presente estudo foi avaliar a influência da fase sigma na resistência à corrosão em microrregiões de juntas soldadas multipasse da liga AISI 316L produzidas pelo processo MIG nos modos de transferência metálica pulsado, curto-circuito e spray. A metodologia consistiu em reproduzir amostras soldadas com parâmetros de soldagem aplicados na indústria para os modos de transferência metálica de interesse, com detalhada caracterização microestrutural da zona fundida de cada condição de soldagem. Em seguida, foram conduzidos ensaios eletroquímicos de corrosão em microrregiões da junta soldada em solução de 3,5% NaCl, e a influência da fase sigma na corrosão por pite foi avaliada por ensaio de imersão em solução de cloreto férrico (6% FeCl3). Caracterizou-se a área exposta à varredura por técnicas de microscopia ótica, microscopia eletrônica de varredura e microanálise química. A soldagem no modo pulsado resultou em uma zona fundida com microestrutura bifásica com a mais baixa fração volumétrica de ferrita delta, de refinada morfologia e isenta de fase sigma, proporcionando o mais nobre desempenho nos ensaios de corrosão, que se manifestou pelo mecanismo de corrosão localizada. A avaliação da área exposta à varredura demonstrou que, previamente a corrosão por pite, a corrosão incia-se de forma localizada, contudo, sem corrosão preferencial de uma das fases, característica que proporcionou parâmetros eletroquímicos mais nobres do que aqueles com corrosão seletiva de fases. Está característica é atribuída à ausência da fase sigma na microestrutura da zona fundida do modo pulsado. No modo curto-circuito ocorreu à decomposição eutetóide da ferrita delta formando a austenita secundária e a fase sigma, sendo está última precipitada principalmente no interior da ferrita delta. A morfologia da corrosão se dá, na fase inicial, como corrosão seletiva de fases, com degradação preferencial da austenita secundária e em direção a ferrita delta, devido à fragilização desta fase pela precipitação de fase sigma em seu interior. A degradação seletiva das fases austenita secundária e ferrita delta causam danos localizados ao filme passivo e, nestas regiões empobrecidas de cromo e molibdênio, ocorre à corrosão por pite. O modo spray com a mais elevada energia de soldagem resultou em uma ferrita delta grosseira e com estreitas bandas de austenita na microrregião de enchimento do chanfro e na raiz da solda, com alto índice de fase sigma nestas localizações. O processo corrosivo da zona fundida caracterizou-se por corrosão seletiva da fase austenita secundária e em direção à matriz austenítica, uma vez que a fase sigma revestiu a ferrita delta, tornando-a a região de comportamento catódico entre o par galvânico formado entre as fases austenita e ferrita delta. A corrosão seletiva da matriz austenítica causa a fragilização localizada do filme passivo com consequente corrosão por pite. O trabalho realizado permite concluir que o potencial de pite foi reduzido com a presença de fase sigma e fases a esta associada, e justamente o modo pulsado obteve destacada resistência à corrosão em função da ausência da fase sigma em sua microestrutura. / Industrial plant designs with asepsis and corrosion resistance requirements have austenitic stainless steels as engineering materials, and the AISI 316L alloy is widely used. The welding of thick plates is performed by MIG processes and the qualification of the welding procedure is carried out based on mechanical properties, insufficient evaluation for applications that require a resistant passive film. The microstructure of the molten zone of the AISI 316L alloy influences the corrosion resistance, and it is necessary to define the mechanisms that govern the influence of the sigma phase on corrosion resistance. In this context, the aim of the present study was to evaluate the influence of the sigma phase on the corrosion resistance in microrregions of multipass welded joints of the AISI 316L alloy produced by MIG process with metal transfer in pulsed, short circuit and spray modes. The methodology consisted in reproducing welded samples with welding parameters applied in the industry for the modes of metallic transfer of interest, with detailed microstructural characterization of the molten zone of each welding condition. Then, electrochemical corrosion tests were carried out in microrregions of the welded joint in 3.5% NaCl solution, and the influence of the sigma phase on pitting corrosion was evaluated by immersion test in ferric chloride solution (6% FeCl3). The area exposed to the scanning was characterized by optical microscopy, scanning electron microscopy and chemical microanalysis. Pulsed mode welding resulted in a molten zone with a biphasic microstructure with the lowest volume fraction of delta ferrite, refined morphology and sigma phase free, providing the noblest performance in the corrosion tests, which occurred in the form of localized corrosion. The evaluation of the area exposed to the scan showed that, prior to pitting corrosion, the corrosion started in a localized manner, however, without preferential corrosion of one of the phases, a characteristic that gave better electrochemical parameters than those with selective corrosion of phases. This characteristic is attributed to the absence of the sigma phase in the microstructure of the molten zone of the pulsed mode. In the short-circuit mode, the eutectoid decomposition of the delta ferrite formed the secondary austenite and the sigma phase, the latter being mainly precipitated inside the delta ferrite. The corrosion morphology occurs in the initial phase as selective corrosion of phases, with preferential degradation of the secondary austenite and towards the ferrite delta, due to the embrittlement of this phase by the precipitation of the sigma phase inside. The selective degradation of the secondary austenite and delta ferrite phases causes localized damage to the passive film and, in these impoverished regions of chromium and molybdenum, occurs to pitting corrosion. The spray mode with the highest welding energy resulted in a coarse delta ferrite with narrow bands of austenite in the chamfer filling microrregion and at the root of the weld, with a high sigma phase index at these locations. The corrosive process of the molten zone was characterized by selective corrosion of the secondary austenite phase and towards the austenitic matrix, since the sigma phase covered the delta ferrite, making it the region of cathodic behavior between the galvanic pair formed between the austenite and ferrite delta phases. Selective corrosion of the austenitic matrix causes localized embrittlement of the passive film with consequent pitting corrosion. The study accomplished allows concluding that the pitting potential was reduced with the presence of sigma phase and phases associated with it, and precisely the pulsed mode obtained outstanding corrosion resistance due to the absence of the sigma phase in its microstructure.

A multi-analytical approach based on in-situ and ex-situ local probing techniques was employed to investigate localized corrosion mechanisms of some aluminum alloys in chloride containing solutions, focusing on the influence of intermetallic particles (IMPs) in the alloys. In the EN AW-3003 alloy, SEM-EDS analysis revealed constituent and dispersoid IMPs. There are two types of constituent IMPs, with size ranging from 0.5 to several μm, and composition typically Al6(Fe,Mn) or Al12(Mn,Fe)3Si, respectively,having a Mn/Fe ratio of about 1:1. Fine dispersoids of 0.5 μm or less in size normally have the composition Al12Mn3Si1-2. Scanning Kelvin probe force microscopy (SKPFM measurements showed that the constituent IMPs have a higher Volta potential compared to the matrix, and the Volta potential difference increased with particle size, probably related to the composition of the IMPs. The SKPFM results also showed a Volta potential minimum in the boundary region adjacent to some larger IMPs. The open-circuit potential and electrochemical impedance spectroscopy measurements indicated local electrochemical activities occurring on the surface, and active-like dissolution in the acidic solutions, but a passive-like behavior in the near-neutral solutions. Infrared reflection-absorption spectroscopy measurements after exposure and thermodynamic calculations suggested the formation of mixtures of aluminum oxyhydroxide and acetate on the surface in acetic acid solutions. The formation and fraction of dominant species of the corrosion products depend on the pH of the solution, and aluminum chloride compounds may form at very low pH. Moreover, an integrated in-situ atomic force microscopy (AFM) and scanningelectrochemical microscopy (SECM) set-up was used to investigate the localized activities on the surface. With a dual mode probe, acting as both AFM tip and SECM microelectrode, concurrent topography and electrochemical current images were obtained on the same area of the surface. Numerical simulations of the SECM suggested a micrometer lateral resolution under favorable conditions and the ability to resolve μmsized active sites with a separation distance of about 3 μm or larger. The simulations were verified by SECM mapping of the aluminum alloys in the chloride solutions. The AFM/SECM measurements revealed enhanced cathodic activity on some larger IMPs and local anodic dissolution around larger IMPs. In-situ AFM monitoring confirmed preferential dissolution in the boundary region adjacent to some of these IMPs. The results elucidate the micro-galvanic effect and size effect of the IMPs during the initiation of localized corrosion of the Al alloys. Furthermore, differences in corrosion properties between EN AW-3003 and a newly developed Al–Mn–Si–Zr alloy were studied with a similar approach. Compared to EN AW-3003, the new alloy had a smaller number of particles with a large Volta potential difference relative to the matrix. In slightly corrosive solutions extensive localized dissolution and deposition of corrosion products occurred on EN AW-3003, whereas only a small number of corroding sites and “tunnel-like” pits occurred on the Al–Mn–Si–Zr alloy. The lower corrosion activity and the smaller tunnel-like pits resulted in lower material loss of the Al–Mn–Si–Zr alloy, which is beneficial for applications using a thin material. / QC 20100702

The corrosion behaviour of cast Al-Mg alloy A535 and its composites containing 10 wt.% and 15 wt.% fly ash, and 10 wt.% hybrid reinforcement (5 wt.% fly ash + 5 wt.% SiC) was investigated using weight-loss and electrochemical corrosion tests, optical microscopy, Scanning Electron Microscopy (SEM) and Energy Dispersive X-ray Spectroscopy (EDS). The tests were conducted in fresh water collected from the South Saskatchewan River and 3.5 wt.% NaCl solution at room temperature. The pH of the salt solution varied from 3 to 9. For comparison, two other aluminum alloys, AA2618 and AA5083-H116, were tested in the same electrolytes. The results of the weight-loss corrosion test showed that unreinforced A535 alloy had a lower corrosion rate in fresh water and seawater environments than the composites at all the tested pH values. The corrosion rate of the composites increased with increasing fly ash content. As expected, the corrosion rates of A535 alloy and the composites tested in fresh water were lower than those in salt solution. The results of the potentiodynamic and cyclic polarization electrochemical tests showed that the corrosion potential (Ecorr) and pitting potential (Epit) of the alloy were more positive than those of the composites. The corrosion and pitting potentials of the composites became more negative (active) with increasing fly ash content. The composites showed more positive (noble) repassivation or protection potential (Erp) than the matrix alloy, with the positivity increasing with fly ash content. Analysis of the electrochemical noise data showed that pitting corrosion was the dominant mode of corrosion for the alloy in 3.5 wt.% NaCl solution. Optical microscopy and SEM revealed that Mg2Si phase and Al-Mg intermetallics corroded preferentially to the matrix. The EDS data indicated that the protective oxide film formed on A535 contained Al2O3 and MgO.

The corrosion behaviour of cast Al-Mg alloy A535 and its composites containing 10 wt.% and 15 wt.% fly ash, and 10 wt.% hybrid reinforcement (5 wt.% fly ash + 5 wt.% SiC) was investigated using weight-loss and electrochemical corrosion tests, optical microscopy, Scanning Electron Microscopy (SEM) and Energy Dispersive X-ray Spectroscopy (EDS). The tests were conducted in fresh water collected from the South Saskatchewan River and 3.5 wt.% NaCl solution at room temperature. The pH of the salt solution varied from 3 to 9. For comparison, two other aluminum alloys, AA2618 and AA5083-H116, were tested in the same electrolytes. The results of the weight-loss corrosion test showed that unreinforced A535 alloy had a lower corrosion rate in fresh water and seawater environments than the composites at all the tested pH values. The corrosion rate of the composites increased with increasing fly ash content. As expected, the corrosion rates of A535 alloy and the composites tested in fresh water were lower than those in salt solution. The results of the potentiodynamic and cyclic polarization electrochemical tests showed that the corrosion potential (Ecorr) and pitting potential (Epit) of the alloy were more positive than those of the composites. The corrosion and pitting potentials of the composites became more negative (active) with increasing fly ash content. The composites showed more positive (noble) repassivation or protection potential (Erp) than the matrix alloy, with the positivity increasing with fly ash content. Analysis of the electrochemical noise data showed that pitting corrosion was the dominant mode of corrosion for the alloy in 3.5 wt.% NaCl solution. Optical microscopy and SEM revealed that Mg2Si phase and Al-Mg intermetallics corroded preferentially to the matrix. The EDS data indicated that the protective oxide film formed on A535 contained Al2O3 and MgO.