The experimental analysis of an autothermal gasoline reformer for use in an auxiliary power unit was undertaken. The development of these auxiliary power units has the potential to create positive economical and environmental benefits. It will provide the necessary energy and heating while utilizing a fuel with a well established infrastructure. Autothermal reforming is a process in which both oxygen and steam are combined with a hydrocarbon fuel over a catalyst bed in order to produce a hydrogen rich gas stream. This process utilizes an exothermic partial oxidation reaction to promote the hydrogen efficient, endothermic steam reforming reaction. The main goals of this study were to design and test the operating conditions of a new autothermal reformer and to determine an operational envelope for the reactor. Furthermore, the data collected was used to validate a numerical model of the reactor that would assist in the development of future compact autothermal reformers. A compact autothermal reformer has been designed with the capability to produce detailed wall and centerline temperature profiles during operation. During the experimental phase of this project, a strong relationship between the main input variables (the oxygen to carbon and steam to carbon ratios) and the performance characteristics of the reactor was found. For the range of experimental conditions tested, the highest molar percent of hydrogen in the reformate for a gas hourly space velocity of 20,000h-1 was found at an oxygen to carbon ratio of 1.0 and a steam to carbon ratio of 2.0. Performance characteristics used for the reactor were the lower heating value, the percent hydrogen yield and fuel conversion, and were found to have maximum values of 46.0%, 47.6% and 67.7% respectively. Carbon deposition on the catalyst bed was found to be significant under certain operating conditions, but had a very small effect on the final conditions of the ATR. The computational fluid dynamics model was shown to have fairly accurate predictions for the temperature profiles as well as the reformate compositions when compared to the experimental data. A number of recommendations have been made to the experimental and numerical studies. It is likely that if employed in future testing, they would improve the overall performance of the compact autothermal reformer. / Thesis (Master, Mechanical and Materials Engineering) -- Queen's University, 2008-04-23 17:14:46.198

The development of an auxiliary power unit (APU) capable of providing climate control and electricity in long haul trucks is of significant interest due to the expected economic and environmental benefits. A potentially efficient and environmentally friendly APU design is one based on the use of an autothermal fuel reformer that converts on-board truck fuel to a hydrogen rich gas that directly fuels a solid oxide fuel cell unit. To assist in the development of such a unit a numerical study of the autothermal reforming of iso-octane in a compact tubular reactor has been undertaken. This was done to determine the reactor performance and the factors that potentially influence its performance. Variations in the wall thermal conductivity, the catalyst thermal conductivity, the catalyst porosity, the conditions of the inlet reactant gas, and the effectiveness factor of the chemical reaction mechanism have been studied to determine their effects on the performance of the reformer. It has been found that higher thermal conductivities of the outer wall and in the catalyst region gave increased dry hydrogen yield and fuel conversion. The study of the effects of inlet species concentration ratios indicated that maximum hydrogen yield was obtained with an oxygen-to-fuel ratio between 1.0 and 1.15 and a steam-to-fuel ratio of approximately 3.0. Results obtained with various inlet species temperatures and bed porosities showed only small changes in the reformer performance. While the results obtained here do provide useful information about the performance of the autothermal reformer, the model used has been re-assessed and it is recommended that an improved model be used in future work. In particular, the assumed effectiveness factors for all of the chemical reactions occurring in the catalyst region need to be improved. This was highlighted by the fact that a brief study indicated a very strong dependence of the reformer product gas composition on the effectiveness factor. This indicates that while the present model is able to predict trends in the reformer performance, it is limited in its accuracy due to the fact that the effectiveness factor used is only approximately known. / Thesis (Master, Mechanical and Materials Engineering) -- Queen's University, 2007-08-31 13:22:27.466

This thesis reports the outcome of a simulation study that examines the feasibility of using hydrogen peroxide as an alternative oxidant in the autothermal reforming (ATR) of diesel. The primary objective is to compare hydrogen peroxide's performance against conventional oxidants in reforming, focusing on product distribution and three pivotal process properties: diesel conversion, hydrogen production, and ethylene generation. The study further investigates the influence of the heat of decomposition on the performance and reaction routes of different oxidants. Additionally, a comparative analysis is conducted on the reforming performance in different reformer configurations, specifically contrasting a combined-reformer-configuration with a catalytic-reformer configuration. The ANSYS Chemkin-Pro is utilized to understand the potential benefits and challenges of the proposed approached. A reduced chemical mechanism of N-heptane/Toluene reforming as a surrogate for diesel, combined with a detailed surface reaction mechanism of propene on a three-way Pt/Rh catalyst are used in this study. It is found that the use of hydrogen peroxide as an oxidant demonstrated a complete fuel conversion and 183% higher hydrogen yield when compared with conventional oxidants. It also led to a 12% lower generation of ethylene, a precursor for coke formation. The catalytic-reformer configuration showed superior performance over the combined-reformer-configuration in terms of hydrogen yield. The insights from this study offer valuable perspectives on the feasibility and efficiency of using hydrogen peroxide as an alternative oxidant in the ATR of diesel, paving the way for potential advancements in the field.

Fuel cell is one of the most promising clean energy and alternative energy technologies due to its advantages of low emissions and high efficiency. One application of the fuel cell technology is onboard auxiliary power units (APUs) for power generation in aircrafts, ships, and automobiles. In order to supply hydrogen or syngas for the fuel cell APUs, onboard fuel processing technology was proposed to convert hydrocarbon fuels into syngas through reforming reactions. Two major tasks need to be completed in onboard fuel processing technology. Firstly sulfur compounds have to be removed from hydrocarbon fuels because sulfur can cause reforming catalyst deactivation and fuel cell electrodes poisoning problems. Secondly hydrogen and carbon monoxide shall be produced by reforming of hydrocarbon fuels at a high energy conversion efficiency. This dissertation focused on onboard fuel processing of Jet-A fuel to produce hydrogen and syngas for solid oxide fuel cell (SOFC) APUs. Jet-A fuel was studied because it is the logistic fuel commonly used for civilian airplanes and military heavy duty trucks. Ultra-deep adsorptive desulfurization of Jet-A fuel from over 1,000 ppmw to below 50 ppmw, and autothermal reforming of n-dodecane as a Jet-A fuel surrogate as well as the real desulfurized Jet-A fuel to produce syngas have been systematically investigated in the present study. For the adsorptive desulfurization of Jet-A fuel, a novel NiO-CeO₂/A1₂O₃-SiO₂ adsorbent was proposed and prepared in-house for experimental tests. The sulfur adsorption kinetic characteristic and isotherm at equilibrium were studied in batch tests, and the dynamic desulfurization performance of the adsorbent was investigated in fixed bed tests. Fixed bed tests operation conditions including liquid hourly space velocity (LHSV), adsorbent particle size, and fixed bed dimensions were optimized to achieve the highest adsorbent sulfur adsorption capacity. For the reforming of Jet-A fuel, autothermal reforming (ATR) method was employed and a bimetallic NiO-Rh catalyst was synthesized for the ATR reactions. A lab-scale 2.5 kWt autothermal reforming system including the reformer and balance-of-plant was designed, fabricated, integrated and tested. The reforming system performances at various operation conditions were compared. Reformer operation temperature, steam to carbon ratio and oxygen to carbon ratio, as well as pre-heating temperatures for fuel, air and steam were optimized based on system energy conversion efficiency, H₂ selectivity and COₓ selectivity.

L'hydrogène pourrait jouer un rôle prépondérant dans le domaine de l'énergie dans les années à venir. De nos jours, la production d'hydrogène provient majoritairement de ressources fossiles. En vue de l'impact néfaste de l'utilisation de ressources fossiles sur l'environnement, produire de l'hydrogène à partir de ressources renouvelables présente un grand intérêt. Dans cette étude, le reformage autotherme du biogaz, une source renouvelable de méthane, a été étudié sur des catalyseurs au nickel à 700°C et à pression atmosphérique. Cette étude porte sur un biogaz modèle composé à 60% de méthane et 40% de dioxyde de carbone mis en présence d'oxygène et de vapeur d'eau dans les proportions : 42% H2O, 14% CH4, 9% CO2, 7% O2 dilués dans l'argon. Dans un premier temps, un criblage de catalyseurs au nickel a été réalisé grâce à un montage composé de 6 réacteurs parallèles. L'outil a permis de montrer qu'un catalyseur bimétallique NiRh supporté sur un spinelle de magnésium était actif et très stable, montrant une conversion totale du méthane après 200h de réaction. L'équivalent de ce catalyseur sans Rh s'est désactivé après seulement 2h de réaction. Notre étude a démontré que cette désactivation était causée par la formation du spinelle de nickel, NiAl2O4. Cette formation est une conséquence des hautes températures présentes dans la zone de combustion qui induisent un désordre dans la structure cristalline du support et permettent, en présence de NiO, la diffusion de ions Ni2+ dans les lacunes du support. Enfin, une étude cinétique a été menée sur des catalyseurs structurés. Un modèle cinétique a été développé, permettant également de décrire le profil de désactivation causée par la perte de sites actifs / Hydrogen is expected to play an increasingly important role in the energy sector in the years to come. Nowadays, hydrogen is mainly produced from fossil fuels. The extensive use of fossil fuels is unsustainable and therefore, hydrogen production from renewable sources is of great interests. Autothermal reforming of biogas, a renewable source of methane, was studied over nickel catalysts at 700°C and at atmospheric pressure. This study focused on model biogas composed of 60% methane and 40% carbon dioxide, reacting with oxygen and steam respecting the composition: 42% H2O, 14% CH4, 9% CO2, 7% O2 diluted in argon. First and foremost, a screening of different catalyst compositions was carried out with a six parallel-flow reactor set-up. This high-throughput technology showed that a NiRh bimetallic catalyst supported on magnesium spinel was active and very stable, still fully converting methane after 200 hours of reaction. On the other hand, its noble-metal free equivalent deactivated after only 2 hours. Our study showed that deactivation was caused by the formation of nickel spinel NiAl2O4. Its formation is a consequence of the exothermicity of the combustion reaction taking place at the catalyst inlet. The high temperatures induce a disorder in the crystal structure of the support and, in presence of NiO, Ni2+ ions can then diffuse into the vacancies of the support. The inactive NiAl2O4 phase is formed. Finally, a kinetic study was performed on structured catalysts. A kinetic model was developed, which also allowed the description of the deactivation profile caused by the loss of active sites

Le reformage autothermique, dans lequel une oxydation air carburant permet d’initier les réactions de formation d’hydrogène à partir de carburant et d’eau, semble une voie prometteuse pour la synthèse d’hydrogène à bord de navires. Son application au diesel, carburant majoritairement utilisé dans le secteur maritime, bien que moins bien connue académiquement que celle du méthane, permet une opérabilité du vaisseau sur l’ensemble du globe. Cependant les réacteurs associés sont particulièrement sujets au dépôt de carbone, néfaste pour leur durabilité, et requièrent alors une attention toute particulière au niveau des zones de mélange lors de leur conception. Dans les cas d’écoulements fortement tridimensionnels, une approche RANS couplée à un schéma cinétique décrivant les espèces gazeuses, est le plus souvent utilisée. Ce schéma consiste alors soit en un nombre succint de réactions empiriques, au risque de se montrer peu précis sur les niveaux de polluants, ou au contraire en des schémas d’une cinquantaine d’espèces issus de la réduction automatique de schémas complets, qui restent cependant trop lourds à utiliser lors d’une phase de conception. L’objectif de la thèse est alors de proposer une méthodologie pour décrire l’impact d’une géométrie sur les niveaux de polluants compatibles avec les outils habituellement utilisés dans le milieu industriel. Ainsi, la description du couplage chimie-écoulement est réalisée par le biais des logiciels Fluent R et de la suite Chemkin R de ANSYS R . Après une analyse de la chimie du reformage autothermique du diesel, une méthode de génération de schémas globaux d’une di-zaine d’espèces à partir d’un schéma détaillé est proposée. Elle est, par la suite appliquée avec succès à l’oxydation partielle du n-dodécane. Le schéma estalors utilisé dans la première simulation réactive de reformeur auto-thermique avec injection de diesel liquide réalisée à ce jour. Malgré les difficultés de validation dûes au manque de données experimentales et aux limitations des logiciels imposés, les résultats obtenus sont encourageants. / Autothermal reformers use fuel-air oxidation to ensure production of hydrogen from fuel and water on-board. The use of diesel instead of better-known methan, permits the ships to be refuelled all around the world. These systems show strong sensitivity to carbon deposit which reduces their lifetime. Good knowledge of the fuel air mixing is thus required. Academic description of such tridimensional systems usually relies on the application of a RANS simulation coupled with gaseous chemical kinetics mechanism. These mechanisms can then consist on a few empirical reactions, or at the opposite, on quite large schemes, with more than 50 species derived automatically from big detailled schemes. The resulting description is then not enough precise, or at the opposite too computationally expensive to be used during design process. This thesis thus aims to develop an industrial compatible methodology to describe the impact of design geometry on pollutant formation. ANSYS software such as Fluent and Chemkin are then used to perform the simulation. An original method of limited size mechanism derivation from larger chemical scheme is proposed. It is succesfully applied to the generation of a partial oxidation mechanism of n-dodecane, from the results of diesel reforming chemical analysis. The resulting scheme is then applied on theliquid injection diesel autoreformer reactive simulation. Even if validation difficulties result from the lack of experimental data and limitations of the softwares, it remains the first simulation of this kind in the litterature, to our knowledge. Promising results are obtained.

No description available.

Le syngas est un mélange gazeux de CO et H2 qui constitue un intermédiaire important dans l’industrie pétrochimique. Plusieurs approches sont utilisées pour le produire. L’oxydation partielle non catalytique (POX) et le reformage à la vapeur (SMR) en font partie. Le reformage auto thermique du méthane (ATR) combine quant à lui ces deux procédés au sein d’un même réacteur. L’amélioration du rendement global du procédé ATR requiert une meilleure caractérisation du comportement des gaz au sein de la chambre. La simulation numérique apparaît comme un outil efficace pour y parvenir. Pour réduire le coût CPU, c'est généralement l'approche RANS (Reynolds Average Numerical Simulation) qui est privilégiée pour la simulation complète de la chambre. Cette approche repose sur l'utilisation de modèles, parmi lesquels le modèle de combustion turbulente, qui a pour objectif de représenter les interactions entre la turbulence et la réaction chimique au sein du mélange. Plusieurs stratégies ont été proposées pour le calculer, qui bénéficient globalement d'une large expérience pour les systèmes classiques mettant en jeu la combustion. Cependant, les flammes observées dans les réacteurs ATR présentent des propriétés assez différentes de ces configurations classiques. La validité des modèles de combustion turbulente classiques doit donc y être vérifiée. L'objectif de cette thèse est de répondre à ce besoin, en testant la validité de différents modèles de combustion turbulente. La première partie du travail a consisté à analyser les propriétés des flammes CH4/O2 enrichies en vapeur d'eau à haute pression, et a notamment permis le développement d’une méthode d’évaluation des temps caractéristiques d’un système chimique. Dans un deuxième temps, une expérience numérique à l’aide d’un code DNS a été réalisée, afin de servir de référence pour tester a priori sur des configurations ATR plusieurs modèles RANS de combustion turbulente couramment utilisés dans le milieu industriel. / Syngas is a gaseous mixture mainly composed of CO and H2, which constitutes a major feedstock in petrochemical industry. Several industrial approaches are commonly used to produce it. Non catalytic Partial Oxidation (POX) and Steam Methane Reforming (SMR) are two of them. Autothermal Reforming (ATR) is a third process that combines both POX and SMR in the same reactor. A better knowledge of the reactive flow properties inside the chamber is required in order to improve the ATR process efficiency. Numerical simulation appears as an efficient tool to reach this goal. Because of the high CPU cost required for these simulations, RANS (Reynolds Average Numerical Simulation) formulation is usually preferred for the simulation of the whole chamber. This approach relies on the use of models, like the turbulent combustion model that aims at describing the interactions between turbulence and chemical reactions. Several approaches have been proposed to compute it, which benefit from a relatively wide experience for the simulation of classical combustion systems. However, ATR flames have some specific properties that make them quite different from these classical configurations, especially because of high pressure, reactants dilution with water and high global equivalence ratio. The validity of classical turbulent combustion models therefore requires to be assessed in ATR configurations. The objective of this thesis is to meet this need by testing the validity of several turbulent combustion models. The first part of this work has been to analyze water-enriched CH4/O2 flames properties at high pressure. In particular, a strategy for evaluating characteristic chemical time scales of a reactive system has been proposed within this context. In a second part, a DNS numerical experiment has been performed. Its results are then used as a benchmark for a priori testing several turbulent combustion models in the context of ATR reactor RANS simulations.

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>