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Hydrodynamic Characteristics (hydrodynamic + characteristic)
Selected AbstractsHydrodynamic Characteristics of a Powder-Particle Spouted Bed with Powder Entrained in Spouting GasTHE CANADIAN JOURNAL OF CHEMICAL ENGINEERING, Issue 4 2005Qunyi Zhu Abstract Spouting of 3.7 mm polyvinyl chloride particles in a cone-based cylindrical column is subjected to entrainment of FCC powder in the spouting air. It is found that the powder entrainment reduces the minimum spouting velocity, increases the bed pressure drop and reduces the maximum spoutable bed height. At any given bed height and value of U/Ums, there is a critical value of powder loading ratio above which spouting gives way to slugging. Le jaillissement de particules de chlorure de polyvinyle dans une colonne cylindrique à base conique a été soumis à un entraînement de poudre de FCC dans l'air jaillissant. On a trouvé que l'entraînement de poudre réduisait la vitesse de jaillissement minimale, augmentait la perte de charge de lit et réduisait la hauteur maximum de lit jaillissant. À toute hauteur de lit et valeur de U/Ums données, il existe une valeur critique du rapport de charge de poudre au-dessus duquel le jaillissement conduit au pistonnage. [source] Hydrodynamic characteristics of gas,solid fluidization at high temperatureTHE CANADIAN JOURNAL OF CHEMICAL ENGINEERING, Issue 1 2010Shabnam Sanaei Abstract Effect of temperature on the hydrodynamics of bubbling gas,solid fluidized beds was investigated in this work. Experiments were carried out at different temperatures ranged of 25,600°C and different superficial gas velocities in the range of 0.17,0.78,m/s with sand particles. The time-position trajectory of particles was obtained by the radioactive particle tracking technique at elevated temperature. These data were used for determination of some hydrodynamic parameters (mean velocity of upward and downward-moving particles, jump frequency, cycle frequency, and axial/radial diffusivities) which are representative to solids mixing through the bed. It was shown that solids mixing and diffusivity of particles increases by increasing temperature up to around 300°C. However, these parameters decrease by further increasing the temperature to higher than 300°C. This could be attributed to the properties of bubble and emulsion phases. Results of this study indicated that the bubbles grow up to a maximum diameter by increasing the temperature up to 300°C, after which the bubbles become smaller. The results showed that due to the wall effect, there is no significant change in the mean velocity of downward-moving clusters. In order to explain these trends, surface tension of emulsion between the rising bubble and the emulsion phase was introduced and evaluated in the bubbling fluidized bed. The results showed that surface tension between bubble and emulsion is increased by increasing temperature up to 300°C, however, after that it acts in oppositely. L'effet de la température sur l'hydrodynamique de lits fluidisés de gaz-solide bouillonnants a fait l'objet de l'étude de cet ouvrage. Des expériences ont été faites à différentes températures se situant entre 25 et 600°C et différentes vélocités de gaz superficiels sur une plage de 0,17 à 0,78,m/s avec particules de sable. La trajectoire temps-position des particules a été obtenue à l'aide d'une technique de repérage par particules radioactives à haute température. Ces données ont été utilisées pour déterminer certains des paramètres hydrodynamiques (vélocité moyenne des particules ascendantes et descendantes, la fréquence de sauts bonds, la fréquence de cycles et les diffusivités axiales et radiales), lesquels sont représentatifs de solides se mélangeant dans le lit. Il a été démontré que le mélange de solides et la diffusivité des particules augmentent en haussant la température à environ 300°C. Cependant, ces paramètres diminuent en accroissant davantage la température au-delà de 300°C. Cela pourrait être attribué aux propriétés des phases de bouillonnement et d'émulsion. Les résultats de cette étude indiquent que les bulles croissent pour atteindre un diamètre maximum en augmentant la température jusqu'à 300°C. Au-delà de cette température, les bulles deviennent plus petites. Les résultats démontrent qu'en raison de l'effet de paroi, il n'y a pas de changement significatif à la vélocité moyenne des grappes descendantes. Afin d'expliquer ces tendances, la tension de surface de l'émulsion entre la bulle ascendante et la phase émulsion a été introduite et évaluée dans le lit fluidisé bouillonnant. Les résultats ont démontré que la tension de surface entre la bulle et l'émulsion augmente en haussant à température jusqu'à 300°C; cependant, après cette température, elle agit inversement. [source] High-performance affinity chromatography with immobilization of protein A and L-histidine on molded monolithBIOTECHNOLOGY & BIOENGINEERING, Issue 5 2002Quanzhou Luo Abstract Reactive monoliths of macroporous poly(glycidyl methacrylate- co -ethylene dimethacrylate) have been prepared by "in-situ" copolymerization of the monomers in the presence of porogenic diluents. Protein A and L-histidine were immobilized on the monoliths directly or through a spacer arm, respectively. The properties of these two kinds of affinity columns were characterized, and the results showed that the columns with coupling of ligands by a spacer arm have some extent of non-specific adsorption for bovine serum albumin. The affinity column based on the monolithic polymer support provided us with good hydrodynamic characteristic, low flow resistance, and easy preparation. These two affinity columns were used for the purification of immunoglobulin G from human serum. The purity of the purified IgG was detected by matrix-assisted laser desorption ionization time-of-flight mass spectrometry (MALDI-TOF-MS). The stability of the protein A affinity column was investigated, and its performance remained invariable after half a year. The effects of the nature and the pH of the buffer system on the adsorption capacity of human IgG on histidyl affinity column were also investigated. The protein A affinity column is favorable for rapid analysis of human IgG samples. In contrast, the advantages of mild elution conditions, high stability, as well as low cost provide the histidyl column further potential possibility for fast removal of IgG from human plasma in clinical applications. © 2002 Wiley Periodicals, Inc. Biotechnol Bioeng 80: 481,489, 2002. [source] Effect of a gas,liquid separator on the hydrodynamics and circulation flow regimes in internal-loop airlift reactorsJOURNAL OF CHEMICAL TECHNOLOGY & BIOTECHNOLOGY, Issue 5 2001Jaroslav Klein Abstract The role of the gas,liquid separator on hydrodynamic characteristics in an internal-loop airlift reactor (ALR) was investigated. Both gas holdup and liquid velocity were measured in a 30,dm3 airlift reactor with two different head configurations: with and without an enlarged separator. A magnetic tracer method using a neutrally buoyant magnetic particle as flowfollower was used to measure the liquid velocity in all sections of the internal-loop airlift reactor. Average liquid circulation velocities in the main parts of the ALR were compared for both reactor configurations. At low air flow rates the separator had no influence on gas holdup, circulation velocity and intensity of turbulence in the downcomer and separator. At higher superficial air velocities, however, the separator design had a decisive effect on the hydrodynamic parameters in the downcomer and the separator. On the other hand, the gas holdup in the riser was only slightly influenced by the separator configuration in the whole range of air flow. Circulation flow regimes, characterising the behaviour of bubbles in the downcomer, were identified and the effect of the separator on these regimes was assessed. © 2001 Society of Chemical Industry [source] Thermal and hydrodynamic characteristics of constructal tree-shaped minichannel heat sinkAICHE JOURNAL, Issue 8 2010Yongping Chen Abstract A three-dimensional thermal and hydrodynamic model for constructal tree-shaped minichannel heat sink is developed. The heat and fluid flow in the constructal heat sink with an inlet hydraulic diameter of 4 mm are numerically analyzed, taking into consideration conjugate heat transfer in the channel walls. The pressure drop, temperature uniformity, and coefficient of performance (COP) of the constructal tree-shaped heat sink are evaluated and compared with those of the corresponding traditional serpentine flow pattern. The results indicate that the constructal tree-shaped minichannel heat sinks have considerable advantages over the traditional serpentine flow patterns in both heat transfer and pressure drop. The strong and weak heat flow can be effectively allocated in tree-shaped flow structures; hence, the inherent advantage of uniform temperature on the heating surface in the constructal tree-shaped heat sink is demonstrated. And in tree-shaped flow structures, the local pressure loss due to confluence flow is found to be larger than that due to diffluence flow. In addition, an aluminum constructal tree-shaped minichannel heat sink is fabricated to conduct the verification experiment. The experimentally measured temperature distribution and pressure drop are in agreement with the numerical simulation, which verifies that the present model is reasonable. © 2009 American Institute of Chemical Engineers AIChE J, 2010 [source] CFD modeling and validation of the turbulent fluidized bed of FCC particlesAICHE JOURNAL, Issue 7 2009Jinsen Gao Abstract An experimental and computational study is presented on the hydrodynamic characteristics of FCC particles in a turbulent fluidized bed. Based on the Eulerian/Eulerian model, a computational fluid dynamics (CFD) model incorporating a modified gas-solid drag model has been presented, and the model parameters are examined by using a commercial CFD software package (FLUENT 6.2.16). Relative to other drag models, the modified one gives a reasonable hydrodynamic prediction in comparison with experimental data. The hydrodynamics show more sensitive to the coefficient of restitution than to the flow models and kinetics theories. Experimental and numerical results indicate that there exist two different coexisting regions in the turbulent fluidized bed: a bottom dense, bubbling region and a dilute, dispersed flow region. At low-gas velocity, solid-volume fractions show high near the wall region, and low in the center of the bed. Increasing gas velocity aggravates the turbulent disorder in the turbulent fluidized bed, resulting in an irregularity of the radial particle concentration profile. © 2009 American Institute of Chemical Engineers AIChE J, 2009 [source] Demarcation of a new circulating turbulent fluidization regimeAICHE JOURNAL, Issue 3 2009Xiaobo Qi Abstract Transient flow behaviors in a novel circulating-turbulent fluidized bed (C-TFB) were investigated by a multifunctional optical fiber probe, that is capable of simultaneously measuring instantaneous local solids-volume concentration, velocity and flux in gas-solid two-phase suspensions. Microflow behavior distinctions between the gas-solid suspensions in a turbulent fluidized bed (TFB), conventional circulating fluidized bed (CFB), the bottom region of high-density circulating fluidized bed (HDCFB), and the newly designed C-TFB were also intensively studied. The experimental results show that particle-particle interactions (collisions) dominate the motion of particles in the C-TFB and TFB, totally different from the interaction mechanism between the gas and solid phases in the conventional CFB and the HDCFB, where the movements of particles are mainly controlled by the gas-particle interactions (drag forces). In addition, turbulence intensity and frequency in the C-TFB are significantly greater than those in the TFB at the same superficial gas velocity. As a result, the circulating-turbulent fluidization is identified as a new flow regime, independent of turbulent fluidization, fast fluidization and dense suspension upflow. The gas-solid flow in the C-TFB has its inherent hydrodynamic characteristics, different from those in TFB, CFB and HDCFB reactors. © 2009 American Institute of Chemical Engineers AIChE J, 2009 [source] Examination of the three-dimensional geometry of cetacean flukes using computed tomography scans: Hydrodynamic implicationsTHE ANATOMICAL RECORD : ADVANCES IN INTEGRATIVE ANATOMY AND EVOLUTIONARY BIOLOGY, Issue 6 2007Frank E. Fish Abstract The flukes of cetaceans function in the hydrodynamic generation of forces for thrust, stability, and maneuverability. The three-dimensional geometry of flukes is associated with production of lift and drag. Data on fluke geometry were collected from 19 cetacean specimens representing eight odontocete genera (Delphinus, Globicephala, Grampus, Kogia, Lagenorhynchus, Phocoena, Stenella, Tursiops). Flukes were imaged as 1 mm thickness cross-sections using X-ray computer-assisted tomography. Fluke shapes were characterized quantitatively by dimensions of the chord, maximum thickness, and position of maximum thickness from the leading edge. Sections were symmetrical about the chordline and had a rounded leading edge and highly tapered trailing edge. The thickness ratio (maximum thickness/chord) among species increased from insertion on the tailstock to a maximum at 20% of span and then decreasing steadily to the tip. Thickness ratio ranged from 0.139 to 0.232. These low values indicate reduced drag while moving at high speed. The position of maximum thickness from the leading edge remained constant over the fluke span at an average for all species of 0.285 chord. The displacement of the maximum thickness reduces the tendency of the flow to separate from the fluke surface, potentially affecting stall patterns. Similarly, the relatively large leading edge radius allows greater lift generation and delays stall. Computational analysis of fluke profiles at 50% of span showed that flukes were generally comparable or better for lift generation than engineered foils. Tursiops had the highest lift coefficients, which were superior to engineered foils by 12,19%. Variation in the structure of cetacean flukes reflects different hydrodynamic characteristics that could influence swimming performance. Anat Rec, 290:614,623, 2007. © 2007 Wiley-Liss, Inc. [source] Hydrodynamics of gas,solid fluidization in tapered bedsTHE CANADIAN JOURNAL OF CHEMICAL ENGINEERING, Issue 3 2009J. S. N. Murthy Abstract Gas,solid fluidization has a wide range of industrial applications like catalytic reactions, combustion, gasification, etc. In a number of these applications, there is particle size reduction during the operation leading to severe entrainment and limitation of operating velocity. The various problems associated with particles of different sizes or changing particles sizes could be overcome by adopting tapered beds in fluidization operation. In the present investigation, the fluidization phenomenon in tapered beds has been critically assessed through experimental investigations using particles of different sizes and materials and wide range of apex angles of the vessels. The effect of particle size and apex angle on the fluidization behaviour is clearly brought out which has not been reported so far in literature. The importance of compressive force existing in tapered beds is highlighted. In addition, correlations for all hydrodynamic characteristics, viz. critical fluidization velocity, minimum velocity for full fluidization, maximum velocity for defluidization, peak pressure drop, fluctuation ratio, compressive force, and hysteresis have been developed some of which are proposed for the first time. La fluidisation gaz-solide revêt un vaste éventail d'applications industrielles comme les réactions catalytiques, la combustion, la gazéification, etc. Pour un certain nombre deces applications, il y a une réduction granulométrique durant l'activité menant à un entraînement età une limitation intenses de la vitesse de fonctionnement. Les divers problèmes liés aux particules de dimensions différentes ou aux dimensions de particules changeantes pourraient être surmontésen adoptant les lits coniques dans les activités de fluidisation. Dans le cadre de la présente étude, lephénomène de fluidisation dans les lits coniques a été évalué de façon critique au moyen devérifications expérimentales employant des particules de dimensions et de matières différentes et d'un vaste éventail d'angles de sommet de fluidiseurs. L'effet de la dimension des particules et del'angle des sommets sur le comportement de la fluidisation est nettement mis en évidence, ce quin'a pas été soulevé à venir jusqu'ici dans la documentation. L'importance de la force decompression qui existe dans les lits coniques est mise en évidence. De plus, les corrélations relativement à l'ensemble des caractéristiques hydrodynamiques, c.-à-d. la vitesse de fluidisation critique, la vitesse minimale de fluidisation complète, la vitesse maximale de défluidisation, la chute des pics de pression, le taux de fluctuation, la force de compression et l'hystérésis, ont été élaborées, certaines d'entre elles étant avancées pour la première fois. [source] Modeling And Solving An Engine Intake Manifold With Turbo Charger For Predictive ControlASIAN JOURNAL OF CONTROL, Issue 3 2006Long Xie ABSTRACT In this paper, we build the intake manifold model of an engine with a turbo charger and develop a high speed calculation algorithm for model-based predictive control in real time. The model is built according to the analysis of its thermodynamic and hydrodynamic characteristics and the sampled experiment data. The model equations are presented as a set of differential equations with condition selection (bifurcation) on the right hand side. The switching surface is divided into two parts, sliding and crossing. The sliding mode on the switching surface is analyzed in detail, and a calculation algorithm is proposed to remove illegal crossing caused by the numerical errors on this surface. Also, the control formula and the condition guiding the bifurcation between these two parts are demonstrated. Using this method, we can solve this model over the entire region of input throttle angles, the stability is greatly increased, and the calculation time is greatly reduced for real time control systems. [source] | |||||||||||||