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Due to the remote and dispersed nature of Alberta’s oil wells, it is not economical for the energy industry to capture all of the solution gas produced and as a result, the gas is being flared and vented in significant amounts. The objective of this research is to aid in the conversion of solution gas into dimethyl ether (DME) in a remote location by designing a distillation column that purifies DME and its reaction by-products, carbon dioxide, methanol and water. In order to develop an implementable solution, the distillation equipment must fit inside of a 40-foot shipping container to be transported to remote locations. Given the size constraint of the system, process intensification is the best strategy to efficiently separate the mixture. Several process intensification distillation techniques are explored, including semicontinuous distillation, the dividing wall column (DWC) and a novel semicontinuous dividing wall column (S-DWC). The traditional semicontinuous distillation column purifies DME to fuel grade purity, however the other components are not separated to a high enough grade given the height constrain of the system. The DWC and S-DWC both purify DME to its desired purity along with producing high purity waste streams. The S-DWC purifies the reaction intermediate methanol to a grade slightly higher than the DWC and is pure enough to recycle back to the reactor. An economic comparison is made between the three systems. While the DWC is a cheaper method of producing DME, the trade-off is the purity of the methanol produced. Overall, this research shows that it is possible to purify DME and its reaction by-products in a 40-foot distillation column at a cost that is competitive with Diesel. / Thesis / Master of Applied Science (MASc)

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[pt] A síntese direta de dimetil éter (DME) a partir de gás de síntese é catalisada a partir de catalisadores bifuncionais que possuem duas propriedades: uma hidrogenante que catalisa a formação de metanol a partir de gás de síntese e a outra desidratante que se encarrega da formação do dimetil éter a partir do metanol. Catalisadores bifuncionais com componente hidrogenante baseado em Cu, Zn e Al e componente desidratante baseado na zeólita H-ferrierita foram sintetizados, avaliando-se, o método de preparação, a influência do alumínio no componente hidrogenante e a razão componente desidratante versus componente hidrogenante. Dos diferentes métodos de preparação utilizados: precipitação-deposição, coprecipitação-impregnação e coprecipitação-sedimentação foram os dois últimos que apresentaram melhores resultados na conversão de gás de síntese além de apresentar a formação do precursor do catalisador de síntese de metanol. Os catalisadores foram caracterizados por: absorção atômica, análise térmica gravimétrica, adsorção de N2, difração de raios-x, redução com temperatura programada (RTP), dessorção com temperatura programada de amônia (DTPNH3), dessorção com temperatura programada de hidrogênio (DTP-H2) e microscopia eletrônica de transmissão. Verificou-se que o catalisador bifuncional apresenta um entupimento no volume de poros de aproximadamente 50 por cento. Os resultados dos raios-x identificaram a formação das fases auricalcita, hidrozincita, malaquita e rosacita nos catalisadores com componente hidrogenante baseado em Cu e Zn dos catalisadores com componente hidrogenante baseado em Cu, Zn e Al, e razão atômica Cu/Zn/Al:55/30/15, se observou somente a fase hidrotalcita. A inclusão de alumínio no componente hidrogenante favoreceu a formação de partículas de CuO muito pequenas, conforme observado na microscopia eletrônica de transmissão e difração de raios-x. A análise da DTP-H2 mostrou que os catalisadores preparados por coprecipitação-impregnação apresentam áreas de cobre um pouco maiores. A DTP-NH3 identificou a presença de sítios ácidos de Lewis e de Bronsted que ainda permanecem na H-ferrierita após a preparação do catalisador bifuncional. Sítios ácidos de Bronsted diminuem em maior proporção no catalisador bifuncional quando é preparado pelo método de coprecipitação-impregnação. Os testes catalíticos mostraram não existem grandes diferenças entre os catalisadores bifuncionais preparados por ambos os métodos e que o alumínio no componente hidrogenante não melhora a atividade catalítica destes catalisadores na síntese direta de DME. Concluiu-se que a etapa limitante do processo é a hidrogenação e que esta é dominada pelo cobre e que a H-ferrierita é um excelente componente desidratante pela sua elevada acidez. / [en] The direct synthesis of dimethyl ether from syngas is catalyzed by bifunctional catalysts: the hydrogenation function that catalyzes the methanol formation and the dehydration function to produce dimethyl ether from methanol. Bifunctional catalysts with Cu, Zn and Al as hydrogenation component and Hferrierite zeolite as dehydration component had been synthesized. It was evaluated the method of preparation, the influence of aluminum present in the hydrogenation component and dehydration/hydrogenation component ratio. The coprecipitating impregnation and coprecipitating sedimentation methods were used to form the precursor of hydrogenation component. The catalysts had been characterized by atomic absorption, thermal gravimetry analysis, N2 adsorption, xrays diffraction, TPR, ammonia TPD, hydrogen TPD and transmission electronic microscopy. It was verified that the bifunctional catalyst lost 50 percent of its pore volume. The results of x-rays identified the formation of aurichalcite, hydrozincite, malachite and rosacite phases in the catalyst based on Cu and Zn. However, in the catalyst based on Cu, Zn and Al (for an atomic ratio, Cu/Zn/Al:55/30/15) only the hidrotalcite phase was found. It was observed that the aluminum introduction in the hydrogenation component favors the formation of very small particles of CuO as verified in transmission electronic microscopy and x-rays diffraction. The NH3-TPD identified the presence of Lewis and Bronsted acid sites that still remain in the H-ferrierite after the preparation of the bifunctional catalysts. Bronsted acid sites had an importante decrease in the bifunctional catalysts when it is prepared by the method of coprecipitating impregnation. The catalytic tests showed that the catalysts prepared by the coprecipitating sedimentation method, present higher conversions and DME selectivitys than the prepared by coprecipitating impregnation. The presence of Al in the hydrogenation component doesn`t improve the catalytic activity. It can be concluded that the H-ferrierite is an excellent dehydration component for its high acidity and that the methanol synthesis can be limitant in the process of direct synthesis of DME from syngas.

The role of a protein-repelling coating is to limit the interaction between a device and its physiological environment. Plasma-polymerized-PEG (pp-PEG) surfaces are of great interest since they are known to avoid protein adsorption. and cell attachment. However, in all the studies previously published in the literature, the PEG coatings have been prepared using low pressure processes. In this thesis, we synthesize biocompatible pp-PEG coatings using atmospheric pressure plasma. Two original methods are developed to obtain these pp-PEG films. 1. Atmospheric pressure plasma liquid deposition (APPLD) consists in the injection of the precursor, tetra(ethylene glycol)dimethylether (tetraglyme), by means of a liquid spray, directly in the post-discharge of an atmospheric argon plasma torch. 2. In atmospheric pressure plasma-enhanced chemical vapor deposition (APPECVD), tetraglyme vapors are brought in the post-discharge trough a heating sprinkler. The chemical composition, as well as the non-fouling properties of the APPLD and APPECVD films, are compared to those of PEG coatings synthesized by conventional low pressure plasma processes. In the first part of the study, the effect of the power on the chemical composition of the films has been investigated by infrared reflection absorption spectroscopy (IRRAS), X-ray photoelectron spectroscopy (XPS) and secondary ions mass spectroscopy (SIMS). The surface analysis reveals that for the APPECVD samples, the fragmentation of the precursor increases as the power of the treatment is increased. In other terms, the lower the plasma power is, the higher the “PEG character” of the resulting films is. Indeed, the C-O component (286.5 eV) of the XPS C 1s peak is decreasing while the hydrocarbon component (285 eV) is increasing as the power of the plasma is increased. The same conclusion can be drawn from the signature ToF-SIMS peaks (m/z = 45 (CH3OCH2+ and +CH2CH2OH), 59 (CH3OCH2CH2+), 103 (CH3(OCH2CH2)2+)) that are decreasing in the case of high power treatments. Accordingly, IRRAS measurements show that the C-O stretching band is decreasing for high power plasma deposition. This is in agreement with the observations made from the analysis of the LP PECVD coatings and from the literature. The films deposited by the APPLD process do not show the same behavior. Indeed, whatever the power injected into the discharge is, we are able to achieve films with a relatively high PEG character (83 %). The second part of this study is dedicated to the evaluation of the non-fouling properties of the coatings by exposing them to proteins (bovine serum albumin and human fibrinogen) and cells (mouse fibroblasts (L929 and MEF)) and controlling the adsorption with XPS (proteins) and SEM (cells). For the APPECVD samples, a low plasma power (30 W) leads to an important reduction of protein adsorption and cell adhesion (over 85%). However, higher-powered treatments tend to reduce the non-fouling ability of the surfaces (around 50% of reduction for a 80 W deposition). The same order of magnitude (over 90% reduction of the adsorption) is obtained for the APPLD surfaces, whatever is the power of the treatment. Those results show an important difference between the two processes in terms of power of the plasma treatment, and a strong relationship between the surface chemistry and the adsorption behavior: the more the PEG character is preserved, the more protein-repellent and cell-repellent is the surface. / Le rôle d’une couche empêchant l’adsorption de protéines est de limiter les interactions entre un implant et le milieu physiologique auquel il est exposé. Les films de poly(éthylène glycol) polymérisés par plasma (pp-PEG) sont d’intérêt majeur car ils sont connus pour empêcher l’adsorption de protéines ainsi que l’attachement cellulaire. Cependant, dans toutes les études publiées précédemment, les couches de type PEG ont été réalisées sous vide. Dans cette thèse de doctorat, nous synthétisons des couches de type pp-PEG biocompatibles par plasmas à pression atmosphérique. A cette fin, deux méthodes originales ont été développées. 1. La première méthode consiste en l’injection du précurseur, le tetra(éthylène glycol) diméthyl éther (tetraglyme), en phase liquide, en nébulisant ce dernier au moyen d’un spray, directement dans la post-décharge d’une torche à plasma atmosphérique fonctionnant à l’argon. En anglais, nous appelons ce procédé « Atmospheric pressure plasma liquid deposition (APPLD) ». 2. Dans la deuxième méthode, appelée en anglais « Atmospheric pressure plasma-enhanced chemical vapor deposition (APPECVD)», le tetraglyme est amené en phase vapeur dans la post-décharge, au moyen d’un diffuseur chauffant. La composition chimique des dépôts de type APPLD et APPECVD, ainsi que leurs propriétés d’anti-adsorption sont évaluées, et comparées aux dépôts pp-PEG obtenus par les méthodes à basse pression conventionnelles. Dans la première partie de cette étude, nous nous focalisons sur la composition chimique des films déposés, et plus particulièrement sur l’influence de la puissance injectée dans le plasma sur cette composition chimique. A cette fin, nous avons fait appel à des techniques d’analyse telles que la spectroscopie de réflexion-absorption infrarouge (IRRAS), la spectroscopie des photoélectrons X (XPS) et la spectrométrie de masse des ions secondaires (SIMS). Il en ressort que les films de type APPECVD perdent progressivement leur « caractère PEG » à mesure que la puissance de la décharge plasma est élevée. Cela serait dû à une plus grande fragmentation du précurseur dans la post-décharge d’un plasma plus énergétique. Cette tendance est cohérente avec ce que nous avons observé pour les dépôts à basse pression ainsi que dans la littérature. Dans le cas des films de type APPLD, un tel comportement n’a pas été mis en évidence : quelle que soit la puissance dissipée dans le plasma, les films présentent un « caractère PEG » relativement élevé. La deuxième partie de cette thèse est dédiée à l’évaluation des propriétés d’anti-adsorption des films synthétisés, en les exposant à des protéines (albumine de sérum bovin et fibrinogène humain) et des cellules (fibroblastes de souris, L929 et MEF). L’adsorption de protéines est contrôlée par XPS tandis que l’attachement cellulaire est contrôlé par imagerie SEM. Pour les échantillons de type APPECVD, un dépôt à faible puissance (30 W) mène à une importante réduction de l’adsorption de protéines et de cellules (> 85%) tandis qu’à de plus hautes puissances (80 W), l’anti-adsorption est sensiblement diminuée (50% de réduction). Dans le cas des dépôts de type APPLD, quelle que soit la puissance du plasma, une forte diminution de l’adsorption de protéines et de cellules est observée (> 90 %). Ces résultats montrent une différence majeure entre les deux procédés quant à l’influence de la puissance du plasma ainsi qu’une forte relation entre la composition chimique de la surface synthétisée et son pouvoir d’anti-adsorption : plus le « caractère PEG » du dépôt est conservé, plus la surface empêchera l’interaction avec les protéines et les cellules.

Excessive use of fossil fuels shall result in the significant energy problems in the coming century and causes global warming by CO2 emission. Use of petroleum in transportation constitutes the dominant part of total petroleum use. Researches on non-petroleum based, environmentally friendly alternative fuels have been ascended in last decades. Among the alternative fuels, DME has been considered as an attractive fuel alternate due to high cetane number, low PM (particulate matter) and low NOx emission. Synthesis of DME is possible with gasification of biowastes or coal and steam reforming of natural gas. DME is produced in two different methods. In the first method, methanol is formed from the synthesis gas, followed by methanol dehydration to DME. In the second method, called as direct synthesis of DME from synthesis gas, methanol formation and dehydration occurs simultaneously at the same location within the reactor. For the direct synthesis of DME, bi-functional catalysts must be used / one site is responsible for methanol synthesis and other site is responsible for methanol dehydration. Throughout this thesis work, several catalysts were prepared to be used as methanol synthesis component or methanol dehydration component of bi-functional direct DME synthesis catalyst and bi-functional catalysts were also prepared for the direct synthesis of DME from synthesis gas. Materials were characterized by XRD, EDS, SEM, N2 physisorption, and DRIFTS characterization techniques. Activity tests were conducted in a high pressure, fixed bed flow reactor at 50 bar and for the feed gas compositions of H2:CO=50:50 and H2:CO: CO2=50:40:10. Addition of zirconia and alumina promoters, long aging time, calcination temperature of 550 &deg / C and reduction at 250 &deg / C were found to be beneficial in methanol synthesis from the equimolar composition of CO and H2. Precipitated catalysts were usually active and selective to methanol. However, bi-functional co-precipitated catalyst was not successful in situ conversion of methanol into dimethyl ether. Furthermore, tungstosilisic acid impregnated SBA-15 was physically mixed with commercial methanol reforming catalyst and activity results revealed that high DME yield and selectivity were obtained. By physically mixing commercial methanol synthesis and reforming catalysts with &gamma / -Al2O3 and TRC-75(L) in appropriate proportions or by preparing the reactor bed in a sequential arrangement, very high DME yields were obtained and superiority of direct synthesis to conventional two step synthesis was proven. Presence of CO2 in the feed stream not only enhanced the catalytic activity but also utilization of the most important greenhouse gas was accomplished. It was seen that synthesized catalysts are very promising in the direct synthesis of dimethyl ether from synthesis gas.

Autoignition and oxidation of two Methane (CH4) and Dimethyl Ether (CH3OCH3 or DME) mixtures in air were studied in shock tubes over a wide range of equivalence ratios at elevated temperatures and pressures. These experiments were conducted in the reflected shock region with pressures ranging from 0.8 to 35.7 atmospheres, temperatures ranging from 913 to 1650 K, and equivalence ratios of 2.0, 1.0, 0.5, and 0.3. Ignition delay times were obtained from shock-tube endwall pressure traces for fuel mixtures of CH4/CH3OCH3 in ratios of 80/20 percent volume and 60/40 percent volume, respectively. Close examination of the data revealed that energy release from the mixture is occurring in the time between the arrival of the incident shock wave and the ignition event. An adjustment scheme for temperature and pressure was devised to account for this energy release and its effect on the ignition of the mixture. Two separate ignition delay correlations were developed for these pressure- and temperature-adjusted data. These correlations estimate ignition delay from known temperature, pressure, and species mole fractions of methane, dimethyl ether, and air (0.21 O2 + 0.79 N2). The first correlation was developed for ignition delay occurring at temperatures greater than or equal to 1175 K and pressures ranging from 0.8 to 35.3 atm. The second correlation was developed for ignition delay occurring at temperatures less than or equal to 1175 K and pressures ranging from 18.5 to 40.0 atm. Overall good agreement was found to exist between the two correlations and the data of these experiments. Findings of these experiments also include that with pressures at or below ten atm, increased concentrations of dimethyl ether will consistently produce faster ignition times. At pressures greater than ten atmospheres it is possible for fuel rich mixtures with lower concentrations of dimethyl ether to give the fastest ignition times. This work represents the most thorough shock tube investigation for oxidation of methane with high concentration levels of dimethyl ether at gas turbine engine relevant temperatures and pressures. The findings of this study should serve as a validation for detailed chemical kinetics mechanisms.

Heavy-duty trucks are in idle operation during long periods of time, providing the vehicles with electricity via the alternator at standstill. Idling trucks contribute to large amounts of emissions and high fuel consumption as a result of the low efficiency from fuel to electricity. Auxiliary power units, which operate independently of the main engine, are promising alternatives for supplying trucks with electricity. Fuel cell-based auxiliary power units could offer high efficiencies and low noise. The hydrogen required for the fuel cell could be generated in an onboard fuel reformer using the existing truck fuel. The work presented in this thesis concerns hydrogen generation from transportation fuels by autothermal reforming focusing on the application of fuel cell auxiliary power units. Diesel and dimethyl ether have been the fuels of main focus. The work includes reactor design aspects, preparation and testing of reforming catalysts including characterization studies and evaluation of operating conditions. The thesis is a summary of five scientific papers. Major issues for succeeding with diesel reforming are fuel injection, reactant mixing and achieving fuel cell quality reformate. The results obtained in this work contribute to the continued research and development of diesel reforming catalysts and processes. A diesel reformer, designed to generate hydrogen to feed a 5 kWe polymer electrolyte fuel cell has been evaluated for autothermal reforming of commercial diesel fuel. The operational results show the feasibility of the design to generate hydrogen-rich gases from complex diesel fuel mixtures and have, together with CFD calculations, been supportive in the development of a new improved reformer design. In addition to diesel, the reforming reactor design was shown to run satisfactorily with other hydrocarbon mixtures, such as gasoline and E85. Rh-based catalysts were used in the studies and exhibit high performance during diesel reforming without coke formation on the catalyst surface. An interesting finding is that the addition of Mn to Rh catalysts appears to improve activity during diesel reforming. Therefore, Mn could be considered to be used to decrease the noble metal loading, and thereby the cost, of diesel reforming catalysts. Dimethyl ether is a potential diesel fuel alternative and has lately been considered as hydrogen carrier for fuel cells in truck auxiliary power units. The studies related to dimethyl ether have been focused on the evaluation of Pd-based catalysts and the influence of operating parameters for autothermal reforming. PdZn-based catalysts were found to be very promising for DME reforming, generating product gases with high selectivity to hydrogen and carbon dioxide. The high product selectivity is correlated to PdZn interactions, leading to decreased activity of decomposition reactions. Auxiliary power systems fueled with DME could, therefore, make possible fuel processors with very low complexity compared to diesel-fueled systems. The work presented in this thesis has enhanced our understanding of diesel and DME reforming and will serve as basis for future studies. / QC 20100804

<p>Heavy-duty trucks are in idle operation during long periods of time, providing the vehicles with electricity via the alternator at standstill. Idling trucks contribute to large amounts of emissions and high fuel consumption as a result of the low efficiency from fuel to electricity. Truck manufacturers are working to develop equipment using auxiliary power units to supply the trucks with electricity, which operate independently of the main engine. Fuel cell-based auxiliary power units could offer high efficiencies and low noise and vibrations. The hydrogen required for the fuel cell can be generated in an onboard fuel reformer. This thesis is devoted to hydrogen generation from dimethyl ether, DME, by autothermal reforming focusing on the application of fuel cell auxiliary power units. In the search for alternative fuels, DME has lately been identified as a promising diesel substitute.</p><p>The first part of the thesis gives an introduction to the field of DME reforming with a literature survey of recent studies within the area. Included are also results from thermodynamic equilibrium calculations.</p><p>In the following parts of the thesis, experimental studies on autothermal reforming of DME are presented. A reformer constructed to generate hydrogen to feed a 5 kW_e polymer electrolyte fuel cell is evaluated with emphasis on trying to work close to a practically viable process, i.e. without external heating and using gas mixtures resembling real conditions. Additional experiments have been conducted to investigate the use of catalytic oxidation of dimethyl ether as a heat source during startup. The results of these studies are presented in Paper I.</p><p>In the second experimental study of this thesis, which is presented in Paper II, Pd-based monolithic catalysts are evaluated at small scale for use in autothermal reforming of DME. A screening of various catalyst materials has been performed followed by a study of the influence on the product composition of varying operating parameters such as oxygen-to-DME ratio, steam-to-DME ratio, and temperature.</p>