Reactive burn models and ignition & growth concept
|
|
|
- Lucinda Lloyd
- 10 years ago
- Views:
Transcription
1 EPJ Web of Conferences 10, (2010) DOI: /epjconf/ c Owned by the authors, published by EDP Sciences, 2010 Reactive burn models and ignition & growth concept R. Menikoff a and M.S. Shaw b Los Alamos National Laboratory, USA Abstract. Plastic-bonded explosives are heterogeneous materials. Experimentally, shock initiation is sensitive to small amounts of porosity, due to the formation of hot spots (small localized regions of high temperature). This leads to the Ignition & Growth concept, introduced by Lee and Tarver in 1980, as the basis for reactive burn models. A homogenized burn rate needs to account for three meso-scale physical effects: (i) the density of active hot spots or burn centers; (ii) the growth of the burn fronts triggered by the burn centers; (iii) a geometric factor that accounts for the overlap of deflagration wavelets from adjacent burn centers. These effects can be combined and the burn model defined by specifying the reaction progress variable λ = g(s) as a function of a dimensionless reaction length s(t) = r bc /l bc, rather than by specifying an explicit burn rate. The length scale l bc (P s ) = [N bc (P s )] 1/3 is the average distance between burn centers, where N bc is the number density of burn centers activated by the lead shock. The reaction length r bc (t) = t 0 D(P(t ))dt is the distance the burn front propagates from a single burn center, where D(P) is the deflagration speed as a function of the local pressure and t is the time since the shock arrival. A key implementation issue is how to determine the lead shock strength in conjunction with a shock capturing scheme. We have developed a robust algorithm for this purpose based on the Hugoniot jump condition for the energy. The algorithm utilizes the time dependence of density, pressure and energy within each cell. The method is independent of the numerical dissipation used for shock capturing. It is local and can be used in one or more space dimensions. The burn model has a small number of parameters which can be calibrated to fit velocity gauge data from shock initiation experiments. 1 Introduction Plastic-bonded explosives (PBX) are heterogeneous materials consisting of explosive grains of various sizes and shapes, a polymeric binder to hold them together and a small amount of porosity; see Fig. 1. Due to the heterogeneities, shock compression gives rise to localized spatial regions of high temperature known as hot spots. Since chemical reaction rates are strongly temperature dependent, reaction in and around hot spots dominate the burning in a shock-to-detonation transition. Pore collapse is a key hot-spot generation mechanism for shock initiation. Experiments have shown that initiation is sensitive to the meso-scale structure and in particular to porosity. The scale of the heterogeneities in a PBX (tens of microns) is smaller than the cell size that can reasonably be used to simulate a typical high explosive (HE) application. Therefore, a homogenized or volume averaged burn rate is needed to account for the sub-grid burn physics. The underlying hot-spot reaction physics is best described by the Ignition & Growth concept reviewed in sec. 2. We then present a new formulation for a burn rate in sec. 3 that better captures the underlying physics of this concept. A key idea is to base the burn model on the strength of the lead a [email protected] b [email protected] This is an Open Access article distributed under the terms of the Creative Commons Attribution-Noncommercial License 3.0, which permits unrestricted use, distribution, and reproduction in any noncommercial medium, provided the original work is properly cited. Article available at or
2 EPJ Web of Conferences Fig. 1. Polarized light micrograph of PBX 9501; from Skidmore et al. (1998, fig. 4). shock. In sec. 4 we present a robust algorithm based on the Hugoniot jump condition for detecting the lead shock. A comparison of numerical results with velocity gauge data for shock initiation experiments of PBX 9502 are shown in sec. 5. Final remarks and extensions of the model formulation are briefly described in sec Ignition & growth concept Currently available burn models are empirical. They work well only for the limited regime in which they are calibrated. The more physical hot-spot models are based, at least heuristically, on the Ignition & Growth concept introduced by Lee and Tarver in The ignition phase corresponds to the formation of hot spots, their reaction and thermal runaway on a fast time scale. The growth phase corresponds to the subsequent burning from reactive wavelets triggered by the burned hot spots. Typically, hot spots represent a small fraction of the HE volume and almost all of the burning occurs in the growth phase. Leading examples of this type of model, or models that can be interpreted with the ignition and growth concept, along with the form for the burn rate are listed below: i Ignition & Growth model, Lee and Tarver (1980). Rate is a function of local pressure and reaction progress variable. The functional dependence on the reaction progress variable can be interpreted as proportional to the average burn front area of the reactive wavelets emanating from the hot spots. ii DAGMAR, Wackerle et al. (1978) and Anderson et al. (1981). Rate is a function of lead shock pressure, equilibrium mixture temperature and first order in reaction progress variable. Model parameters were calibrated to embedded Manganin stress gauge data. iii JTF model, Johnson et al. (1985). Multi-step reaction with the rates a function of the lead shock pressure, equilibrium mixture pressure and first order in reaction progress variable. Noteworthy for comparison with embedded magnetic velocity gauge data; see Vorthman et al. (1985). iv WSD model, Wescott et al. (2005). This is a generalization of model i above. The shock density is used to switch between rates calibrated to the ignition and propagation regimes. In each regime the rate depends on the local pressure and the reaction progress variable p.2
3 New Models and Hydrocodes for Shock Wave Processes in Condensed Matter v CREST model, Handley (2006). Rate is a function of reactant entropy for two-phase model with pressure but not temperature equilibrium. Two reaction progress variables are used to tune reaction profile based on analysis of embedded magnetic velocity gauge data; see James and Lambourn (2006). At the time that the DAGMAR and JTF models were developed, artificial viscosity was used for shock dissipation. The lead shock was determined by scanning the viscous pressure profile for the first local minimum. This algorithm had difficulty when a compressive wave followed the lead shock. Due in part to the numerical issue with robustness, these models never gained favor. The implementation of the WSD model in (Stewart et al. 2007, 2.4) detects the time of arrival of the lead shock based on the maximum t P for each cell. Then a level set algorithm applied to the shock arrival time is used to determine the shock speed, which determines the shock state. This may not be too accurate but is good enough to use as a switch on the initiation regime or growth regime. For the CREST model, the solid entropy can be thought of as a measure of the lead shock strength since the chemical energy released is apportioned to the products. There are issues with shock capturing in two-phase models since the component energy equations are not in conservation form; see Petitpas et al. (2009) for details. Burn rates based on the lead shock strength naturally account for the phenomena of shock desensitization. With the possible exception of the CREST model, different rate parameters are needed to account for the initial temperature or initial porosity of a PBX. In effect, a PBX at a given initial condition is treated as a distinct explosive. To overcome this and other deficiencies, a burn model needs to better account for the sub-grid or meso-scale burn physics. Based on the ignition and growth concept, three key physical effects need to be incorporated in a burn model: (i) the density of active hot spots or burn centers, which depends on the lead shock strength; (ii) the growth of burn fronts triggered by burn centers, which depends on the local deflagration speed; (iii) a geometric factor that accounts for the overlap of deflagration wavelets from adjacent burn centers, which depends on material heterogeneities that determine the distribution of hot spots. 3 New formulation For our formulation, Scaled Unified Reactive Front (SURF) model, the volume average of the hot-spot reaction is accounted for by directly specifying the reaction progress variable λ as a function of time. The effective burn rate is then determined implicitly as R = (d/dt)λ. (1) The key point is that burn centers are formed and reaction begins only after the lead shock pass over potential hot spot sites; such as a void or an embedded high density particle. Moreover, the average amount of burn depends on the distribution of hot spots, whether a hot spot evolves into a burn center and how a burn center interacts with its neighbors. First, let us define the shock functions t s (x) = time the lead shock arrives at point x, P s (x) = pressure of lead shock at point x. We express the reaction progress variable as λ(t, P s, P) = 0, for t t s; g ( s(t t s, P s, P) ) (2), for t > t s ; where P(x, t) = local pressure, g(s) = reaction scale function, s(t, Ps, P) = scaled burn center reaction length = r bc (t, P)/l bc (Ps), r bc (t, P) = reaction length for single burn center, l bc (Ps) = distance between burn centers p.3
4 EPJ Web of Conferences For now we neglect the initial hot-spot volume, and express the reaction length for a single burn center as t r bc (t, P) = D ( P(t ) ) dt, (3) t s which depends on the local deflagration speed, D(P). The average distance between burn centers can be written l bc (Ps) = [N bc (P s )] 1/3, (4) where N bc (P s ) is the number density of burn centers or those hot spots activated by the lead shock that burn on a fast time scale. We expect the reaction scale function g to depend on the statistical distribution of hot spots. It accounts for the interaction of burn centers and the geometric factor for the burn front area due to the overlap of burn wavelets from each burn center. For a given PBX composition, g would depend on the structure of heterogeneities grain size distribution, morphology, imperfections, impurities, voids that give rise to hot spots. To summarize the SURF model: it is determined by specifying three functions g(s), N bc (P s ) and D(P) that separate the sub-grid burning into distinct parts, each of which has a clear physical interpretation. 3.1 Fitting forms For independent randomly distributed point burn centers in three dimensions, the reaction scale function can be shown to be g(s) = 1 exp( s 3 ); see Nichols and Tarver (2002) and Hill et al. (2009). This includes the geometric effects of outward hot-spot burning and inward grain burning similar to the functional dependence of the burn rate on the reaction progress variable, λ 2/3 (1 λ) 2/3, in the original ignition & growth model of Lee and Tarver (1980). The geometry of burn wavelets triggered by the burn centers depends on the dissipative mechanism generating the hot spots. We use a form corresponding to cylindrical burn centers g(s) = 1 exp( s 2 ). (5) Measurements on the regression rate for propellants and higher pressure measurements with diamond anvil cells, see for example Esposito et al. (2003), suggest that the deflagration speed is proportional to the pressure. We express it as D(P) = D(P s ) (P/P s ) n. (6) The sensitivity of distance-to-detonation with shock pressure suggests that the number of burn centers rises rapidly with shock strength. We use a shock strength factor of the form f (P s ) = D(P s ) [N bc (P s )] 1/3 = exp [ A + B min(p s, P s,max )/P ref ] t 1 ref, (7) where P ref and t ref are units for pressure and time. The scaled reaction length is then expresses as t s = f (P s ) [P(t )/P s ] n dt. (8) t s For these choices, the SURF model has only 4 parameters (A, B, P s,max, n). The model can be calibrated to shock initiation experiments by fitting to embedded velocity gauge data; i.e., Lagrangian time histories of the particle velocity for several points along a shock-to-detonation trajectory; for details see Shaw and Menikoff (2010). We note that s = 1 corresponds to 1 e-fold of reaction. The time scale for this to occur is roughly τ = 1/ f (P s ), and the corresponding burn center length scale l bc = D(P s )/ f (P s ). For PBX 9502, used to illustrate the model in sec. 5, the reaction time scale for a shock-to-detonation transition varies p.4
5 New Models and Hydrocodes for Shock Wave Processes in Condensed Matter Fig. 2. Hugoniot locus and shock profile in (V, P)-plane. Also shown are Rayleigh line and isentrope thru shocked state. Fig. 3. Evolution of pressure profiles (series of fixed times) and lead shock pressure (dashed red curve) from shock detector for cases with decaying (left) and strengthening (right) shocks. between 10 ns and 1 μs. Assuming D(P s ) is on the order of 0.1mm/μs, the burn center length scale would be between 1 and 100 microns. This is comparable to the grain size for the PBX. The effective burn rate for the fitting form corresponding to Eq. (5) can be expressed as R(λ, P, P s ) = d dt λ = d ds g d dt s = 2[ ln(1 λ)] 1/2 (1 λ) f (P s ) [P/P s ] n (9) since s 2 = ln (1 λ). We note that the λ dependence of the rate is very similar to that in the CREST model; see (Handley and Lambourn 2009, Eq. (2)). Moreover, Eqs. (5) and (8) are similar to the history variable reactive burn model in the CTH code; see description in (Starkenberg 2002). 4 Lead shock detection algorithm A numerical shock profile mimics that of a steady-state solution to the Euler equations with viscosity and heat conduction. In the (V, P)-plane, the continuum profile lies between the Rayleigh line and the Hugoniot locus, as shown in Fig. 2; see Gilbarg (1951). The distance between a point on a shock profile and the Hugoniot locus is roughly proportional to the Hugoniot function, h(v, e) = e e (V 0 V)[P(V, e) P 0 ], (10) whose zero level set defines the Hugoniot locus. The subscript 0 denotes the state ahead of the shock. For the lead shock, the ahead state is well defined; the ambient or initial state of the HE. For a given cell in a numerical simulations, the shock state can be determined by calculating the time dependent Hugoniot function, h(t) = h ( (V(t), e(t) ), (11) p.5
6 EPJ Web of Conferences Fig. 4. Comparison of embedded velocity gauge data for shock initiation experiments in PBX 9502; shots 2s57 (13.5 GPa) and 2s68 (11.5 GPa) from Gustavsen et al. (2006). Solid lines are experimental data and dashed lines are simulations. Gague positions are shown in the legend of each plot. and looking for either a zero crossing or a local minimum. The former case occurs when the shock is followed by a compression wave and the latter when the shock is followed by an expansion wave. Following waves would cause the shock strength to change and the wave front to either accelerate or deaccelerate. The ability of the algorithm to detection the lead shock is shown in Fig. 3. In this example, a piston is used to drive a shock in non-reacting PBX An accelerating piston strengthens the lead shock, while a deaccelerating piston causes the shock to decay. The algorithm works equally well for the case in which reaction accelerates the lead shock. Possibly the error in one of the other shock jump conditions, such as, δ = (u s u 0 ) 2 (P s P 0 )(V 0 V s ), can be used to estimate the error in the shock state. Three key features of the shock detection algorithm are: (i) It is independent of the numerical dissipation and can be used with a shock capturing algorithm based on either artificial viscosity or a Riemann solver, i.e., Godunov scheme. (ii) It is local to a cell and independent of the shock direction, hence can be applied in one or more space dimensions. (iii) It determines time of shock arrival along with the shock state. Consequently, the shock detection algorithm is well suited for our model formulation. 5 Numerical results for PBX 9502 To illustrate the effectiveness of the SURF model for shock initiation we compare simulated results with data from gas gun experiments. A series of shock-to-detonation experiments were carried out on PBX 9502 by Gustavsen et al. (2006) in which the initial shock pressure was varied. The gas gun drives a well supported planar shock in the PBX. Hence the flow is one dimensional. Embedded magnetic velocity gauges were used to measure Lagrangian time histories for up to ten particles. This provides information on the flow behind the lead shock as well as the trajectory of the lead wave. Numerical simulations were performed utilizing the Amrita framework Quirk (1998a,b). The solver algorithm is a Godunov scheme on a 1-D Lagrangian mesh. Both the projectile from the gas gun and the PBX were included in the calculation. The measured projectile velocity was used as the initial condition to set the initial shock pressure. Adaptive mesh refinement allowed shock fronts and the reacting regions to be well resolved. A noteworthy point of the shock detection algorithm is that the Hugoniot function variable h enabled the refinement criterion to select the finest mesh for the lead shock, and to prevent reaction from occurring in the numerical shock profile. Coarsening the mesh by 1 level behind the lead shock is a smoothing operation that damps out numerical variations in the shock state due to the discretization of the shock profile p.6
7 New Models and Hydrocodes for Shock Wave Processes in Condensed Matter A comparison of the velocity gauge data for two experiments and numerical results are shown in Fig. 4. The initial shock pressure in shot 2s57 is 13.5 GPa and in shot 2s68 is 11.5 GPa. We note that initiation is sensitive to the shock pressure. The relatively small pressure difference (15%), changes the transition time from 1.3 μs to greater than 2.0 μs (50%). In addition, the timing of the jump off velocity of the gauges depends on the shock velocity. Hence accurate equations of state are needed for the reactants and products of the PBX. The one we are using is described in (Menikoff 2009). A noteworthy feature of the data is displayed by the first gauge which is at the PBX interface. After the shock, the particle velocity is nearly constant. This is compatible with a small initial hot-spot volume and burning resulting from the subsequent growth of the hot-spot reaction length; i.e., r bc (t, P). This is qualitatively different then the original Ignition & Growth model in which the burn rate is a function of the local pressure. We expect that the different behavior for the rate behind the lead shock wouldhavealargeeffect on short-shock initiation experiments. Further details on the SURF model and comparisons with additional experiments can be found in a companion paper of ours (Shaw and Menikoff 2010). 6 Final remarks We have focused on shock initiation. But a burn model needs to deal with two additional detonation phenomenon: (i) The curvature effect for propagating detonation waves. (ii) Change of the ignition sensitivity with the initial state of a PBX. We conclude with a brief comments on incorporating these properties within the context of a hot-spot model. The detonation speed and state of an underdriven planar detonation wave is uniquely determined by the CJ condition and the equation of state of the HE. In general, however, the detonation speed and state depends on the local curvature of the detonation front. This is known as the curvature effect. Due to the jump conditions for a quasi-steady detonation (Menikoff et al. 1996), the curvature effect is sensitive to the reaction zone width. This can lead numerical simulations to have a mesh dependent curvature effect. Typically, the reaction zone width decreases with a finer mesh and results in a smaller numerical curvature effect. Alternatively, the reaction rate of a burn model can be adjusted to tune the reaction zone width in order to fit the curvature effect. In fact, Wescott et al. (2005) fit both regimes for PBX 9502 using a variation of the original Lee & Tarver model; terms were added to the rate which effectively switch from initiation parameters to propagation parameters based on the shock density; see (Wescott et al. 2005, Eqs. (44) and (45)) and (Stewart et al. 2007, 2.4 & 2.5.2). We note that the reaction zone for a propagating detonation wave depends on the rate for the lead shock pressures greater than P CJ, while shock initiation depends on lead shock pressures less than P CJ. Thus for our formulation, it would be natural to fit the shock strength factor f (P s ) separately for the two disjoint regimes. Simulations would need the reaction zone to be sufficiently resolved. Very likely adaptive mesh refinement of the detonation front would be needed for efficiency. Initiation sensitivity of a PBX depends on its initial state. Lower initial density increases the shock sensitivity. This is compatible with a higher porosity resulting in an increased number of potential sites for hot spots. In addition, a PBX is more sensitive when hot then when cold. This can be attributed to varying the number of hot spots that become burn centers. Dissipative mechanisms that localize energy in a shocked PBX give rise to a temperature distribution; see for example Menikoff (2004). Hot spots would correspond to the high temperature tail of the distribution. Due to the temperature sensitivity of a chemical rate, burn centers (in which thermal runaway occurs on a fast time scale) can be approximated as those hot spots above a cutoff temperature. A higher initial temperature would shift the temperature distribution resulting in a greater density of burn centers. For our formulation of a hot-spot burn model, the change in sensitivity could be taken into account by modifying the shock strength factor to depend on the initial state as well as the shock pressure; i.e., f (P s,ρ 0, T 0 ). Finally, we note that all the burn models mentioned in sec. 2 have been calibrated to fit some experimental data. To assess the relative merits of different models one needs to compare each model with a large number of experiments covering a wide range of detonation phenomenon. We think that p.7
8 EPJ Web of Conferences a burn model that incorporates the underlying physics of hot spots is likely to do better than ad hoc fitting forms for the reaction rate. This work was carried out under the auspices of the U. S. Dept. of Energy at LANL under contract DE-AC52-06NA We would like to thank Rick Gustavsen for providing the gauge data from his shock initiation experiments in electronic form. References A. B. Anderson, M. J. Ginsberg, W. L. Seitz, and J. Wackerle. Shock initiation of porous TATB. In Seventh Symposium (International) on Detonation, pages , A. P. Esposito, D. L. Farber, J. E. Reaugh, and J. M. Zaug. Reaction propagation rates in HMX at high pressure. Propellants, Explosives, Pyrotechnics, 28:83 88, D. Gilbarg. The existence and limit behavior of the one-dimensional shock layer. Am.J.Math., 73: , R. L. Gustavsen, S. A. Sheffield, and R. R. Alcon. Measurements of shock initiation in the tri-aminotri-nito-benzene based explosive PBX 9502: Wave forms from embedded gauges and comparison of four different material lots. J. Appl. Phys., 99:114907, C. A. Handley. The CREST reactive burn model. In Thirteenth Symposium (International) on Detonation, pages , C. A. Handley and B. D. Lambourn. Predicting the effect of porosity on the shock sensitivity of explosives. In Shock Compression of Condensed Matter, pages , L. G. Hill, B. Zimmermann, and A. Nichols. On the burn topology of hot-spot initiated reactions. In Shock Compression of Condensed Matter, pages , H. R. James and B. D. Lambourn. On the systematics of particle velocity histories in the shock-todetonation transition regime. J. Appl. Phys., 100:084906, J. N. Johnson, P. K. Tang, and C. A. Forest. Shock-wave initiation of heterogeneous reactive solids. J. Appl. Phys., 57: , E. L. Lee and C. M. Tarver. Phenomenological model of shock initiation in heterogeneous explosives. Phys. Fluids, 23: , R. Menikoff. Complete EOS for PBX Technical Report LA-UR , Los Alamos National Laboratory, R. Menikoff. Pore collapse and hot spots in HMX. In Shock Compression of Condensed Matter 2003, pages , R. Menikoff, K. S. Lackner, and B. G. Bukiet. Modeling flows with curved detonation waves. Combustion and Flame, 104: , A. Nichols and C. Tarver. A statistical hot spot reactive flow model for shock initiation and detonation of solid HE. In Twelfth Symposium (International) on Detonation, pages , F. Petitpas, R. Saurel, E. Franquet, and A. Chinnayya. Modelling detonation waves in condensed energetic materials: Multiphase CJ conditions and multidimensional computations. Shock Waves, 19: , J. J. Quirk. Amrita - a computational facility for CFD modelling. In 29 th Computational Fluid Dynamics, VKI Lecture Series, chapter 4. von Karmen Institute, 1998a. J. J. Quirk. AMR sol: Design principles and practice. In 29 th Computational Fluid Dynamics, VKI Lecture Series, chapter 5. von Karmen Institute, 1998b. M. S. Shaw and R. Menikoff. Reactive burn model for shock initiation in a PBX: Scaling and separability based on the hot spot concept. In Fourteenth Symposium (International) on Detonation, C. B. Skidmore, D. S. Phillips, J. T. Mang, and J. A. Romero. The evolution of microstructural changes in pressed HMX explosives. In Eleventh Symposium (International) on Detonation, pages , J. Starkenberg. Modeling detonation propagation and failure using explosive initiation models in a conventional hydrocode. In Twelfth Symposium (International) on Detonation, pages , p.8
9 New Models and Hydrocodes for Shock Wave Processes in Condensed Matter D. S. Stewart, S. Yoo, and B. L. Wescott. High-order numerical simulation and modelling of the interaction of energetic and inert materials. Combustion Theory and Modelling, 11: , J. Vorthman, G. Andrews, and J. Wackerle. Reaction rates from electromagnetic gauge data. In Eighth Symposium (International) on Detonation, pages , J. Wackerle, R. L. Rabie, M. J. Ginsberg, and A. B. Anderson. A shock initiation study of PBX In Actes du Symposium International sur le Comportement des Milieux Denses sour Hautes Pression Dynamiques, pages , B. L. Wescott, D. S. Stewart, and W. C. Davis. Equation of state and reaction rate for condensed-phase explosives. J. Appl. Phys., 98:053514, p.9
CFD Based Air Flow and Contamination Modeling of Subway Stations
CFD Based Air Flow and Contamination Modeling of Subway Stations Greg Byrne Center for Nonlinear Science, Georgia Institute of Technology Fernando Camelli Center for Computational Fluid Dynamics, George
Flow in data racks. 1 Aim/Motivation. 3 Data rack modification. 2 Current state. EPJ Web of Conferences 67, 02070 (2014)
EPJ Web of Conferences 67, 02070 (2014) DOI: 10.1051/ epjconf/20146702070 C Owned by the authors, published by EDP Sciences, 2014 Flow in data racks Lukáš Manoch 1,a, Jan Matěcha 1,b, Jan Novotný 1,c,JiříNožička
Calculation of Combustion, Explosion and Detonation Characteristics of Energetic Materials
Calculation of Combustion, Explosion and Detonation Characteristics... 97 Central European Journal of Energetic Materials, 2010, 7(2), 97-113 ISSN 1733-7178 Calculation of Combustion, Explosion and Detonation
MOLECULAR DYNAMICS SIMULATION OF DYNAMIC RESPONSE OF BERYLLIUM
MOLECULAR DYNAMICS SIMULATION OF DYNAMIC RESPONSE OF BERYLLIUM Aidan P. Thompson, J. Matthew D. Lane and Michael P. Desjarlais Sandia National Laboratories, Albuquerque, New Mexico 87185, USA Abstract.
Express Introductory Training in ANSYS Fluent Lecture 1 Introduction to the CFD Methodology
Express Introductory Training in ANSYS Fluent Lecture 1 Introduction to the CFD Methodology Dimitrios Sofialidis Technical Manager, SimTec Ltd. Mechanical Engineer, PhD PRACE Autumn School 2013 - Industry
Sound. References: L.D. Landau & E.M. Lifshitz: Fluid Mechanics, Chapter VIII F. Shu: The Physics of Astrophysics, Vol. 2, Gas Dynamics, Chapter 8
References: Sound L.D. Landau & E.M. Lifshitz: Fluid Mechanics, Chapter VIII F. Shu: The Physics of Astrophysics, Vol., Gas Dynamics, Chapter 8 1 Speed of sound The phenomenon of sound waves is one that
ME6130 An introduction to CFD 1-1
ME6130 An introduction to CFD 1-1 What is CFD? Computational fluid dynamics (CFD) is the science of predicting fluid flow, heat and mass transfer, chemical reactions, and related phenomena by solving numerically
CFD SIMULATION OF SDHW STORAGE TANK WITH AND WITHOUT HEATER
International Journal of Advancements in Research & Technology, Volume 1, Issue2, July-2012 1 CFD SIMULATION OF SDHW STORAGE TANK WITH AND WITHOUT HEATER ABSTRACT (1) Mr. Mainak Bhaumik M.E. (Thermal Engg.)
High Speed Aerodynamics Prof. K. P. Sinhamahapatra Department of Aerospace Engineering Indian Institute of Technology, Kharagpur
High Speed Aerodynamics Prof. K. P. Sinhamahapatra Department of Aerospace Engineering Indian Institute of Technology, Kharagpur Module No. # 01 Lecture No. # 06 One-dimensional Gas Dynamics (Contd.) We
APPLICATION OF TRANSIENT WELLBORE SIMULATOR TO EVALUATE DELIVERABILITY CURVE ON HYPOTHETICAL WELL-X
PROCEEDINGS, Thirty-Third Workshop on Geothermal Reservoir Engineering Stanford University, Stanford, California, January 8-30, 008 SGP-TR-185 APPLICATION OF TRANSIENT WELLBORE SIMULATOR TO EVALUATE DELIVERABILITY
Modeling and Simulations of Cavitating and Bubbly Flows
Muon Collider/Neutrino Factory Collaboration Meeting Riverside, California, January 27-31, 2004 Modeling and Simulations of Cavitating and Bubbly Flows Roman Samulyak Tianshi Lu, Yarema Prykarpatskyy Center
TESTING AND ANALYSIS OF SURVIVABILITY OF SHAPED-CHARGES IN BULLET IMPACT CONDITIONS
TESTING AND ANALYSIS OF SURVIVABILITY OF SHAPED-CHARGES IN BULLET IMPACT CONDITIONS T. Yarom, R. Ceder, S. Miller, M. Rav-Hon RAFAEL, MANOR - Propulsion & Explosive Systems Division I S R A E L ABSTRACT
A COMBINED EXPERIMENTAL/NUMERICAL METHODOLOGY TO ASSESS THE SENSITIVITY OF PBX's (*)
A COMBINED EXPERIMENTAL/NUMERICAL METHODOLOGY TO ASSESS THE SENSITIVITY OF PBX's (*) Philippe Chabin, Pierre Brunet, Serge Lécume SNPE Propulsion Centre de Recherches du Bouchet BP 2 97 VertlePetit France
Basic Principles in Microfluidics
Basic Principles in Microfluidics 1 Newton s Second Law for Fluidics Newton s 2 nd Law (F= ma) : Time rate of change of momentum of a system equal to net force acting on system!f = dp dt Sum of forces
Hydrodynamics of stellar explosions
Some basic hydrodynamics The art of CFD Hydrodynamic challenges in stellar explosions Hydrodynamics of stellar explosions General: Literature L.D.Landau & E.M.Lifshitz, Fluid Mechanics, Pergamon (1959)
Computational Fluid Dynamics (CFD) and Multiphase Flow Modelling. Associate Professor Britt M. Halvorsen (Dr. Ing) Amaranath S.
Computational Fluid Dynamics (CFD) and Multiphase Flow Modelling Associate Professor Britt M. Halvorsen (Dr. Ing) Amaranath S. Kumara (PhD Student), PO. Box 203, N-3901, N Porsgrunn, Norway What is CFD?
CFD Application on Food Industry; Energy Saving on the Bread Oven
Middle-East Journal of Scientific Research 13 (8): 1095-1100, 2013 ISSN 1990-9233 IDOSI Publications, 2013 DOI: 10.5829/idosi.mejsr.2013.13.8.548 CFD Application on Food Industry; Energy Saving on the
CFD SIMULATION OF NATURAL GAS COMBUSTION AND IST APPLICATION TO TUNNEL KILN FIRING
CFD SIMULATION OF NATURAL GAS COMBUSTION AND IST APPLICATION TO TUNNEL KILN FIRING. R. Obenaus-Emler University of Leoben Contents 1. Intoduction to combustion models in OpenFOAM 2. The Flamelet-Model
NUMERICAL SIMULATION OF REGULAR WAVES RUN-UP OVER SLOPPING BEACH BY OPEN FOAM
NUMERICAL SIMULATION OF REGULAR WAVES RUN-UP OVER SLOPPING BEACH BY OPEN FOAM Parviz Ghadimi 1*, Mohammad Ghandali 2, Mohammad Reza Ahmadi Balootaki 3 1*, 2, 3 Department of Marine Technology, Amirkabir
Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows
Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows 3.- 1 Basics: equations of continuum mechanics - balance equations for mass and momentum - balance equations for the energy and the chemical
Investigation of the Effect of Dynamic Capillary Pressure on Waterflooding in Extra Low Permeability Reservoirs
Copyright 013 Tech Science Press SL, vol.9, no., pp.105-117, 013 Investigation of the Effect of Dynamic Capillary Pressure on Waterflooding in Extra Low Permeability Reservoirs Tian Shubao 1, Lei Gang
Collision of a small bubble with a large falling particle
EPJ Web of Conferences 67, 212 (214) DOI: 1.11/ epjconf/ 21467212 C Owned by the authors, published by EDP Sciences, 214 Collision of a small bubble with a large falling particle Jiri Vejrazka 1,a, Martin
Chapter 29 Scale-Free Network Topologies with Clustering Similar to Online Social Networks
Chapter 29 Scale-Free Network Topologies with Clustering Similar to Online Social Networks Imre Varga Abstract In this paper I propose a novel method to model real online social networks where the growing
NUCLEAR ENERGY RESEARCH INITIATIVE
NUCLEAR ENERGY RESEARCH INITIATIVE Experimental and CFD Analysis of Advanced Convective Cooling Systems PI: Victor M. Ugaz and Yassin A. Hassan, Texas Engineering Experiment Station Collaborators: None
AN EFFECT OF GRID QUALITY ON THE RESULTS OF NUMERICAL SIMULATIONS OF THE FLUID FLOW FIELD IN AN AGITATED VESSEL
14 th European Conference on Mixing Warszawa, 10-13 September 2012 AN EFFECT OF GRID QUALITY ON THE RESULTS OF NUMERICAL SIMULATIONS OF THE FLUID FLOW FIELD IN AN AGITATED VESSEL Joanna Karcz, Lukasz Kacperski
TWO-DIMENSIONAL FINITE ELEMENT ANALYSIS OF FORCED CONVECTION FLOW AND HEAT TRANSFER IN A LAMINAR CHANNEL FLOW
TWO-DIMENSIONAL FINITE ELEMENT ANALYSIS OF FORCED CONVECTION FLOW AND HEAT TRANSFER IN A LAMINAR CHANNEL FLOW Rajesh Khatri 1, 1 M.Tech Scholar, Department of Mechanical Engineering, S.A.T.I., vidisha
How To Model A Horseshoe Vortex
Comparison of CFD models for multiphase flow evolution in bridge scour processes A. Bayón-Barrachina, D. Valero, F.J. Vallès Morán, P. A. López-Jiménez Dept. of Hydraulic and Environmental Engineering
Forces on the Rocket. Rocket Dynamics. Equation of Motion: F = Ma
Rocket Dynamics orces on the Rockets - Drag Rocket Stability Rocket Equation Specific Impulse Rocket otors Thrust orces on the Rocket Equation of otion: = a orces at through the Center of ass Center of
Lecture 6 - Boundary Conditions. Applied Computational Fluid Dynamics
Lecture 6 - Boundary Conditions Applied Computational Fluid Dynamics Instructor: André Bakker http://www.bakker.org André Bakker (2002-2006) Fluent Inc. (2002) 1 Outline Overview. Inlet and outlet boundaries.
SOME EXAMPLES OF ENERGETIC MATERIAL MODELLING WITH LSDYNA
SOME EXAMPLES OF ENERGETIC MATERIAL MODELLING WITH LSDYNA Michel QUIDOT SNPE Propulsion Centre de Recherches du Bouchet BP 2 91710 Vert Le Petit France Email : [email protected] ABSTRACT : SNPE is using
A wave lab inside a coaxial cable
INSTITUTE OF PHYSICS PUBLISHING Eur. J. Phys. 25 (2004) 581 591 EUROPEAN JOURNAL OF PHYSICS PII: S0143-0807(04)76273-X A wave lab inside a coaxial cable JoãoMSerra,MiguelCBrito,JMaiaAlves and A M Vallera
CHEMICAL ENGINEERING AND CHEMICAL PROCESS TECHNOLOGY - Vol. I - Interphase Mass Transfer - A. Burghardt
INTERPHASE MASS TRANSFER A. Burghardt Institute of Chemical Engineering, Polish Academy of Sciences, Poland Keywords: Turbulent flow, turbulent mass flux, eddy viscosity, eddy diffusivity, Prandtl mixing
A software for calculation of optimum conditions for cotton, viscose, polyester and wool based yarn bobbins in a hot-air bobbin dryer
A software for calculation of optimum conditions for cotton, viscose, polyester and wool based yarn bobbins in a hot-air bobbin dryer H. Kuşçu, K. Kahveci, U. Akyol and A. Cihan Abstract In this study,
FUNDAMENTALS OF ENGINEERING THERMODYNAMICS
FUNDAMENTALS OF ENGINEERING THERMODYNAMICS System: Quantity of matter (constant mass) or region in space (constant volume) chosen for study. Closed system: Can exchange energy but not mass; mass is constant
MOLECULAR DYNAMICS INVESTIGATION OF DEFORMATION RESPONSE OF THIN-FILM METALLIC NANOSTRUCTURES UNDER HEATING
NANOSYSTEMS: PHYSICS, CHEMISTRY, MATHEMATICS, 2011, 2 (2), P. 76 83 UDC 538.97 MOLECULAR DYNAMICS INVESTIGATION OF DEFORMATION RESPONSE OF THIN-FILM METALLIC NANOSTRUCTURES UNDER HEATING I. S. Konovalenko
CONVERGE Features, Capabilities and Applications
CONVERGE Features, Capabilities and Applications CONVERGE CONVERGE The industry leading CFD code for complex geometries with moving boundaries. Start using CONVERGE and never make a CFD mesh again. CONVERGE
Carbon Cable. Sergio Rubio Carles Paul Albert Monte
Carbon Cable Sergio Rubio Carles Paul Albert Monte Carbon, Copper and Manganine PhYsical PropERTieS CARBON PROPERTIES Carbon physical Properties Temperature Coefficient α -0,0005 ºC-1 Density D 2260 kg/m3
A subgrid-scale model for the scalar dissipation rate in nonpremixed combustion
Center for Turbulence Research Proceedings of the Summer Program 1998 11 A subgrid-scale model for the scalar dissipation rate in nonpremixed combustion By A. W. Cook 1 AND W. K. Bushe A subgrid-scale
Modeling and Simulation of Oil-Water Flows with Viscous Fingering in Heterogeneous Porous Media.
ACMA 2014 Modeling and Simulation of Oil-Water Flows with Viscous Fingering in Heterogeneous Porous Media. H. DJEBOURI 1, S. ZOUAOUI 1, K. MOHAMMEDI 2, and A. AIT AIDER 1 1 Laboratoire de Mécanique Structure
Turbulence Modeling in CFD Simulation of Intake Manifold for a 4 Cylinder Engine
HEFAT2012 9 th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics 16 18 July 2012 Malta Turbulence Modeling in CFD Simulation of Intake Manifold for a 4 Cylinder Engine Dr MK
Fundamentals of Pulse Detonation Engine (PDE) and Related Propulsion Technology
Fundamentals of Pulse Detonation Engine (PDE) and Related Propulsion Technology Dora E. Musielak, Ph.D. Aerospace Engineering Consulting Arlington, TX All rights reserved. No part of this publication may
Model of a flow in intersecting microchannels. Denis Semyonov
Model of a flow in intersecting microchannels Denis Semyonov LUT 2012 Content Objectives Motivation Model implementation Simulation Results Conclusion Objectives A flow and a reaction model is required
12.307. 1 Convection in water (an almost-incompressible fluid)
12.307 Convection in water (an almost-incompressible fluid) John Marshall, Lodovica Illari and Alan Plumb March, 2004 1 Convection in water (an almost-incompressible fluid) 1.1 Buoyancy Objects that are
Modelling and Computation of Compressible Liquid Flows with Phase Transition
JASS 2009 - Joint Advanced Student School, Saint Petersburg, 29. 03. - 07. 04. 2009 Modelling and Simulation in Multidisciplinary Engineering Modelling and Computation of Compressible Liquid Flows with
Development of Thermal Recovery Simulator for Hot Water Flooding
Paper ID 119 ABSTRACT Development of Thermal Recovery Simulator for Hot Water Flooding Shotaro Nihei, Masanori Kurihara Department of Resources and Environmental Engneering, Waseda University, Japan Author
Graduate Certificate Program in Energy Conversion & Transport Offered by the Department of Mechanical and Aerospace Engineering
Graduate Certificate Program in Energy Conversion & Transport Offered by the Department of Mechanical and Aerospace Engineering Intended Audience: Main Campus Students Distance (online students) Both Purpose:
Tomasz STELMACH. WindSim Annual User Meeting 16 June 2011
Developments of PHOENICS as CFD engine for WindSim Tomasz STELMACH Ltd, UK [email protected] WindSim Annual User Meeting 16 June 2011 Topics of presentation 1. - who we are, what we do 2. PHOENICS 3. GCV -
Numerical Model for the Study of the Velocity Dependence Of the Ionisation Growth in Gas Discharge Plasma
Journal of Basrah Researches ((Sciences)) Volume 37.Number 5.A ((2011)) Available online at: www.basra-science -journal.org ISSN 1817 2695 Numerical Model for the Study of the Velocity Dependence Of the
Detonation Waves and Pulse Detonation Engines
Detonation Waves and Pulse Detonation Engines E. Wintenberger and J.E. Shepherd Explosion Dynamics Laboratory, Graduate Aeronautical Laboratories, California Institute of Technology, Pasadena, CA 95 Ae03,
Free Fall: Observing and Analyzing the Free Fall Motion of a Bouncing Ping-Pong Ball and Calculating the Free Fall Acceleration (Teacher s Guide)
Free Fall: Observing and Analyzing the Free Fall Motion of a Bouncing Ping-Pong Ball and Calculating the Free Fall Acceleration (Teacher s Guide) 2012 WARD S Science v.11/12 OVERVIEW Students will measure
Natural Convection. Buoyancy force
Natural Convection In natural convection, the fluid motion occurs by natural means such as buoyancy. Since the fluid velocity associated with natural convection is relatively low, the heat transfer coefficient
Chapter 8 Maxwell relations and measurable properties
Chapter 8 Maxwell relations and measurable properties 8.1 Maxwell relations Other thermodynamic potentials emerging from Legendre transforms allow us to switch independent variables and give rise to alternate
CFD STUDY OF TEMPERATURE AND SMOKE DISTRIBUTION IN A RAILWAY TUNNEL WITH NATURAL VENTILATION SYSTEM
CFD STUDY OF TEMPERATURE AND SMOKE DISTRIBUTION IN A RAILWAY TUNNEL WITH NATURAL VENTILATION SYSTEM J. Schabacker, M. Bettelini, Ch. Rudin HBI Haerter AG Thunstrasse 9, P.O. Box, 3000 Bern, Switzerland
Basic Equations, Boundary Conditions and Dimensionless Parameters
Chapter 2 Basic Equations, Boundary Conditions and Dimensionless Parameters In the foregoing chapter, many basic concepts related to the present investigation and the associated literature survey were
Is This Combustible Dust?
1 of 5 8/6/2012 1:16 PM Is This Combustible Dust? Thursday, 19 July 2012 Dust explosions and fires are serious hazards in the process industries that have lead to loss of life, injury to plant personnel
ACETYLENE AIR DIFFUSION FLAME COMPUTATIONS; COMPARISON OF STATE RELATIONS VERSUS FINITE RATE KINETICS
ACETYLENE AIR DIFFUSION FLAME COMPUTATIONS; COMPARISON OF STATE RELATIONS VERSUS FINITE RATE KINETICS by Z Zhang and OA Ezekoye Department of Mechanical Engineering The University of Texas at Austin Austin,
Differential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation
Differential Relations for Fluid Flow In this approach, we apply our four basic conservation laws to an infinitesimally small control volume. The differential approach provides point by point details of
Part IV. Conclusions
Part IV Conclusions 189 Chapter 9 Conclusions and Future Work CFD studies of premixed laminar and turbulent combustion dynamics have been conducted. These studies were aimed at explaining physical phenomena
1 Foundations of Pyrodynamics
1 1 Foundations of Pyrodynamics Pyrodynamics describes the process of energy conversion from chemical energy to mechanical energy through combustion phenomena, including thermodynamic and fluid dynamic
Supporting document to NORSOK Standard C-004, Edition 2, May 2013, Section 5.4 Hot air flow
1 of 9 Supporting document to NORSOK Standard C-004, Edition 2, May 2013, Section 5.4 Hot air flow A method utilizing Computational Fluid Dynamics (CFD) codes for determination of acceptable risk level
CFD Applications using CFD++ Paul Batten & Vedat Akdag
CFD Applications using CFD++ Paul Batten & Vedat Akdag Metacomp Products available under Altair Partner Program CFD++ Introduction Accurate multi dimensional polynomial framework Robust on wide variety
Understanding Plastics Engineering Calculations
Natti S. Rao Nick R. Schott Understanding Plastics Engineering Calculations Hands-on Examples and Case Studies Sample Pages from Chapters 4 and 6 ISBNs 978--56990-509-8-56990-509-6 HANSER Hanser Publishers,
Numerical Simulation of Pulse Detonation Engine Phenomena
Numerical Simulation of Pulse Detonation Engine Phenomena. He and A. R. Karagozian Department of Mechanical and Aerospace Engineering University of California, Los Angeles, CA 995-597 Abstract This paper
Contents. Microfluidics - Jens Ducrée Physics: Fluid Dynamics 1
Contents 1. Introduction 2. Fluids 3. Physics of Microfluidic Systems 4. Microfabrication Technologies 5. Flow Control 6. Micropumps 7. Sensors 8. Ink-Jet Technology 9. Liquid Handling 10.Microarrays 11.Microreactors
Lecture 9, Thermal Notes, 3.054
Lecture 9, Thermal Notes, 3.054 Thermal Properties of Foams Closed cell foams widely used for thermal insulation Only materials with lower conductivity are aerogels (tend to be brittle and weak) and vacuum
NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES
Vol. XX 2012 No. 4 28 34 J. ŠIMIČEK O. HUBOVÁ NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES Jozef ŠIMIČEK email: [email protected] Research field: Statics and Dynamics Fluids mechanics
Lecture 14. Introduction to the Sun
Lecture 14 Introduction to the Sun ALMA discovers planets forming in a protoplanetary disc. Open Q: what physics do we learn about the Sun? 1. Energy - nuclear energy - magnetic energy 2. Radiation - continuum
Finite Element Modules for Enhancing Undergraduate Transport Courses: Application to Fuel Cell Fundamentals
Finite Element Modules for Enhancing Undergraduate Transport Courses: Application to Fuel Cell Fundamentals Originally published in 2007 American Society for Engineering Education Conference Proceedings
Statistical Forecasting of High-Way Traffic Jam at a Bottleneck
Metodološki zvezki, Vol. 9, No. 1, 2012, 81-93 Statistical Forecasting of High-Way Traffic Jam at a Bottleneck Igor Grabec and Franc Švegl 1 Abstract Maintenance works on high-ways usually require installation
Laminar and Turbulent flow. Flow Sensors. Reynolds Number. Thermal flow Sensor. Flow and Flow rate. R = Mass Flow controllers
Flow and Flow rate. Laminar and Turbulent flow Laminar flow: smooth, orderly and regular Mechanical sensors have inertia, which can integrate out small variations due to turbulence Turbulent flow: chaotic
CFD Simulation of Subcooled Flow Boiling using OpenFOAM
Research Article International Journal of Current Engineering and Technology E-ISSN 2277 4106, P-ISSN 2347-5161 2014 INPRESSCO, All Rights Reserved Available at http://inpressco.com/category/ijcet CFD
THE INSTITUTE FOR SHOCK PHYSICS Understanding Materials at Extreme Dynamic Compression
THE INSTITUTE FOR SHOCK PHYSICS Understanding Materials at Extreme Dynamic Compression Yogendra M. Gupta Washington ate University email: [email protected] Acknowledgements: 1. DOE/NNSA support 2. D. Lacina,
Laboratory scale electrical resistivity measurements to monitor the heat propagation within porous media for low enthalpy geothermal applications
32 CONVEGNO NAZIONALE 19-21 Novembre 2013 TRIESTE Laboratory scale electrical resistivity measurements to monitor the heat propagation within porous media for low enthalpy geothermal applications N. Giordano
The Viscosity of Fluids
Experiment #11 The Viscosity of Fluids References: 1. Your first year physics textbook. 2. D. Tabor, Gases, Liquids and Solids: and Other States of Matter (Cambridge Press, 1991). 3. J.R. Van Wazer et
Lecture 4 Classification of Flows. Applied Computational Fluid Dynamics
Lecture 4 Classification of Flows Applied Computational Fluid Dynamics Instructor: André Bakker http://www.bakker.org André Bakker (00-006) Fluent Inc. (00) 1 Classification: fluid flow vs. granular flow
Science Standard Articulated by Grade Level Strand 5: Physical Science
Concept 1: Properties of Objects and Materials Classify objects and materials by their observable properties. Kindergarten Grade 1 Grade 2 Grade 3 Grade 4 PO 1. Identify the following observable properties
HYBRID ROCKET TECHNOLOGY IN THE FRAME OF THE ITALIAN HYPROB PROGRAM
8 th European Symposium on Aerothermodynamics for space vehicles HYBRID ROCKET TECHNOLOGY IN THE FRAME OF THE ITALIAN HYPROB PROGRAM M. Di Clemente, R. Votta, G. Ranuzzi, F. Ferrigno March 4, 2015 Outline
A.17. OXIDIZING PROPERTIES (SOLIDS)
A.17. OXIDIZING PROPERTIES (SOLIDS) 1. METHOD 1.1. INTRODUCTION It is useful to have preliminary information on any potentially explosive properties of the substance before performing this test. This test
Heating & Cooling in Molecular Clouds
Lecture 8: Cloud Stability Heating & Cooling in Molecular Clouds Balance of heating and cooling processes helps to set the temperature in the gas. This then sets the minimum internal pressure in a core
Fracture and strain rate behavior of airplane fuselage materials under blast loading
EPJ Web of Conferences 6, 6 42017 (2010) DOI:10.1051/epjconf/20100642017 Owned by the authors, published by EDP Sciences, 2010 Fracture and strain rate behavior of airplane fuselage materials under blast
4.3 Results... 27 4.3.1 Drained Conditions... 27 4.3.2 Undrained Conditions... 28 4.4 References... 30 4.5 Data Files... 30 5 Undrained Analysis of
Table of Contents 1 One Dimensional Compression of a Finite Layer... 3 1.1 Problem Description... 3 1.1.1 Uniform Mesh... 3 1.1.2 Graded Mesh... 5 1.2 Analytical Solution... 6 1.3 Results... 6 1.3.1 Uniform
INTRODUCTION TO FLUID MECHANICS
INTRODUCTION TO FLUID MECHANICS SIXTH EDITION ROBERT W. FOX Purdue University ALAN T. MCDONALD Purdue University PHILIP J. PRITCHARD Manhattan College JOHN WILEY & SONS, INC. CONTENTS CHAPTER 1 INTRODUCTION
Abaqus/CFD Sample Problems. Abaqus 6.10
Abaqus/CFD Sample Problems Abaqus 6.10 Contents 1. Oscillatory Laminar Plane Poiseuille Flow 2. Flow in Shear Driven Cavities 3. Buoyancy Driven Flow in Cavities 4. Turbulent Flow in a Rectangular Channel
EVALUATION OF PHOENICS CFD FIRE MODEL AGAINST ROOM CORNER FIRE EXPERIMENTS
EVALUATION OF PHOENICS CFD FIRE MODEL AGAINST ROOM CORNER FIRE EXPERIMENTS Yunlong Liu and Vivek Apte CSIRO Fire Science and Technology Laboratory PO Box 31 North Ryde, NSW 167, Australia TEL:+61 2 949
RESULTS OF ICARUS 9 EXPERIMENTS RUN AT IMRA EUROPE
Roulette, T., J. Roulette, and S. Pons. Results of ICARUS 9 Experiments Run at IMRA Europe. in Sixth International Conference on Cold Fusion, Progress in New Hydrogen Energy. 1996. Lake Toya, Hokkaido,
7. DYNAMIC LIGHT SCATTERING 7.1 First order temporal autocorrelation function.
7. DYNAMIC LIGHT SCATTERING 7. First order temporal autocorrelation function. Dynamic light scattering (DLS) studies the properties of inhomogeneous and dynamic media. A generic situation is illustrated
Overset Grids Technology in STAR-CCM+: Methodology and Applications
Overset Grids Technology in STAR-CCM+: Methodology and Applications Eberhard Schreck, Milovan Perić and Deryl Snyder [email protected] [email protected] [email protected]
Effect of Aspect Ratio on Laminar Natural Convection in Partially Heated Enclosure
Universal Journal of Mechanical Engineering (1): 8-33, 014 DOI: 10.13189/ujme.014.00104 http://www.hrpub.org Effect of Aspect Ratio on Laminar Natural Convection in Partially Heated Enclosure Alireza Falahat
How To Calculate Thermal Resistance On A Pb (Plastipo)
VISHAY BEYSCHLAG Resistive Products 1. INTRODUCTION Thermal management is becoming more important as the density of electronic components in modern printed circuit boards (PCBs), as well as the applied
Explosion Hazards of Hydrogen-Air Mixtures. Professor John H.S. Lee McGill University, Montreal, Canada
Explosion Hazards of Hydrogen-Air Mixtures Professor John H.S. Lee McGill University, Montreal, Canada Hydrogen Safety Issues Wide spread use of hydrogen requires significant efforts to resolve safety
CFD Application on Food Industry; Energy Saving on the Bread Oven
Iranica Journal of Energy & Environment 3 (3): 241-245, 2012 ISSN 2079-2115 IJEE an Official Peer Reviewed Journal of Babol Noshirvani University of Technology DOI: 10.5829/idosi.ijee.2012.03.03.0548 CFD
Numerical Analysis of Independent Wire Strand Core (IWSC) Wire Rope
Numerical Analysis of Independent Wire Strand Core (IWSC) Wire Rope Rakesh Sidharthan 1 Gnanavel B K 2 Assistant professor Mechanical, Department Professor, Mechanical Department, Gojan engineering college,
VARIANCE REDUCTION TECHNIQUES FOR IMPLICIT MONTE CARLO SIMULATIONS
VARIANCE REDUCTION TECHNIQUES FOR IMPLICIT MONTE CARLO SIMULATIONS An Undergraduate Research Scholars Thesis by JACOB TAYLOR LANDMAN Submitted to Honors and Undergraduate Research Texas A&M University
Effect of Pressure Ratio on Film Cooling of Turbine Aerofoil Using CFD
Universal Journal of Mechanical Engineering 1(4): 122-127, 2013 DOI: 10.13189/ujme.2013.010403 http://www.hrpub.org Effect of Pressure Ratio on Film Cooling of Turbine Aerofoil Using CFD Vibhor Baghel
Multi-Block Gridding Technique for FLOW-3D Flow Science, Inc. July 2004
FSI-02-TN59-R2 Multi-Block Gridding Technique for FLOW-3D Flow Science, Inc. July 2004 1. Introduction A major new extension of the capabilities of FLOW-3D -- the multi-block grid model -- has been incorporated
TWO-PHASE FLOW IN A POROUS MEDIA TEST-CASES PERFORMED WITH TOUGH2
TWO-PHASE FLOW IN A POROUS MEDIA TEST-CASES PERFORMED WITH TOUGH2 Paris 23 rd September 2010 E. Treille, J. Wendling Andra C.TR.AEAP.1000xx AGENCE NATIONALE POUR LA GESTION DES DÉCHETS RADIOACTIFS Tough2
Introduction to CFD Basics
Introduction to CFD Basics Rajesh Bhaskaran Lance Collins This is a quick-and-dirty introduction to the basic concepts underlying CFD. The concepts are illustrated by applying them to simple 1D model problems.
