Performance of turbulence models for single phase and liquid-solid slurry flows in pressurized pipe systems

2020 ◽  
Vol 214 ◽  
pp. 107711
Author(s):  
Pelin Ilker ◽  
Mehmet Sorgun
Author(s):  
Ik-Joon Song ◽  
Kyung-Jin Shin ◽  
Jungwoo Kim ◽  
Ik Kyu Park ◽  
Seung-Jun Lee

2020 ◽  
Vol 66 (9) ◽  
pp. 544-553
Author(s):  
Urban Močnik ◽  
Bogdan Blagojevič ◽  
Simon Muhič

A plate heat exchanger with a dimple pattern heat plate has a large number of dimples. The shape of dimples defines the characteristics of the plate heat exchanger. Although such heat exchangers have become increasingly popular due to their beneficial characteristics, knowledge of the flow characteristics in such kind of channel is poor. A good knowledge of the flow conditions inside of such channel is crucial for the successful and efficient development of new products. In this paper single-phase water flow in dimple pattern plate heat exchanger was investigated with application of computational fluid dynamics and laboratory experiments. Numerical analysis was performed with two turbulence models, Realizable - with enhanced wall treatment function and - SST. The first predicts a slightly smaller pressure drop and the second slightly larger compared to the results of laboratory measurements. Our research found that despite the relatively low velocity of the fluid, turbulent flow occurs in the channel due to its shape. We also found that there are two different flow regimes in the micro plate heat exchanger channel. The first regime is the regime that dominates the heat transfer, and the second is the regime where a recirculation zone appears behind the brazing point, which reduces the surface for heat transfer. The size of the second regime does not change significantly with the velocity of the fluid in the volume considered.


Author(s):  
Benny T. Kuan ◽  
M. Philip Schwarz

Single-phase and two-phase (gas-solid) turbulent flow calculations are performed for 90° duct bends having radii of curvature ranging from 1.5 to 2.0 duct diameter, and with either a square or circular cross-section. The considered flow Reynolds number is between 6×104 and 3×105, and the particulate flows examined pertain to two different solid mass loading ratios: 1.5×10−4 and 0.33. Numerous turbulence models have been utilized to simulate the turbulent fluid motion within the duct bend while particle trajectories are calculated on the basis of a Lagrangian approach. Reasonable agreement with the experimental data is achieved for the continuous phase in the cases tested. In contrast, significant disparities with the measurements arise in particle tracking calculations, especially in regions where particle rope dispersion is predominant. Results of this investigation indicate the need for more experimental testing of mill-duct flows of similar configuration in order to facilitate a better understanding and modeling of strongly curved gas-solid duct flows.


2015 ◽  
Author(s):  
R. Broglia ◽  
S. Zaghi ◽  
E. F. Campana ◽  
M. Visonneau ◽  
P. Queutey ◽  
...  

This paper presents CFD validation efforts for the high-speed, multihull Delft Catamaran 372 advancing in calm water with steady drift angles. Available experimental data include hydrodynamic loads (from BSHC), sinkage and trim measurements (from BSHC and CNR-INSEAN), and stereo-PIV measurements on several transverse planes (from CNR-INSEAN). Three organizations from three countries have conducted unsteady Reynolds averaged Navier Stokes (URANS) or Detached Eddy Simulations (DES) by using their own codes: CNR-INSEAN using Xnavis; IIHR, The University of Iowa using CFDShip-Iowa and CNRS/ECN using ISIS. Computations have been made using different grid strategies (structured grid with overlap, unstructured grid with or without an automatic mesh refinement (AMR)), several turbulence models (the isotropic one equation Spalart-Allmaras model, the anisotropic two equations Shear Stress Transport (SST) k and Explicit Algebraic Reynolds Stress Model (EARSM) models, and Detached Eddy Simulations) and different free surface approaches (single phase level set (LS) and volume of fluid (VoF)). Comparisons are made in terms of hydrodynamics loads, local quantities in separated vortex cores (i.e. axial vorticity, axial velocity, position of the vortex and turbulent kinetic energy (TKE)), planar data (velocity field, axial vorticity field and TKE on selected planes) and wave patterns. Discussions and comparisons on the onset and progression of the separated vortical structures are presented. In general computational results have shown that the main features of the separated flow field are well captured by all the computations. No large differences between submissions can be inferred from the cross planar fields; effects of grid resolution and turbulence model have been investigated by the vortex analysis. Grid resolution effects are dominant in the onset region; only very refined grids (total of order of 100M of grid points or using an AMR technique) are able to provide field quantities closer to EFD data. Turbulence model effects are dominant in the progression of the main vortices, with DES simulations and RANS based on non-isotropic models proved to be superior (stronger and less dissipated vortices) than one equation isotropic models. In terms of hydrodynamic loads, a general good agreement between the submissions has been observed (standard deviation on the resistance prediction of about 3.5%). Similar differences between CFD have been seen for the lateral force prediction, whereas larger discrepancy is observed for the yaw moment estimation (about 7%). The comparison with measured data reveals a rather large overall error (of the order of 15%). However, EFD values where collected for different conditions and a larger model; reference values have been obtained by an interpolation procedure on speed/drift plane, whereas no Reynolds number correction was considered. Differences due to grid resolution and the model adopted for the description of the free surface have been also investigated; very fine grids are required to capture wave breaking and rebounds phenomena. Both single phase LS and VoF approaches are able to capture wave induced vortices, some differences are seen in their progression; the VOF method shows the formation of foam close to the free surface region, whereas the LS provides a long life vortices.


2020 ◽  
pp. 1-35
Author(s):  
Rodrigo Petrone dos Anjos ◽  
Ricardo de Andrade Medronho ◽  
Tnia Suaiden Klein

2020 ◽  
Vol 135 (3) ◽  
Author(s):  
Aurélien Bordet ◽  
Sébastien Poncet ◽  
Michel Poirier ◽  
Nicolas Galanis

Author(s):  
Sarada Kuravi ◽  
Krishna M. Kota ◽  
Jianhua Du ◽  
Louis C. Chow ◽  
David P. Colvin

A numerical model to investigate heat transfer characteristics of the MEPCM slurry flow inside a typical microchannel is presented in the paper. The temperature field inside the channel wall is solved three dimensionally and is coupled with the three dimensional velocity and temperature fields of the fluid. The effective specific heat method is used to model the heat sink (MEPCM) in the single phase fluid. The slurry is assumed to be homogeneous with temperature-independent properties. The effects of various parameters such as concentration of MEPCM particles and their size on the heat transfer characteristics of slurry flow are discussed. The results of the numerical model are validated with single phase fluid flow analysis and slurry flows in microchannels separately since no experiment has been performed till date on microsized channels (less than 500 microns in size) employing MEPCM slurry. The analysis would help in designing and optimizing future designs of MEPCM slurry flows in MMC heat sinks.


Author(s):  
Fujun Gan ◽  
Libing Zhu ◽  
Jiazheng Liu ◽  
Yixiong Zheng ◽  
Xing Tong

Computational Fluid Dynamics (CFD) simulation has been increasingly used in Nuclear Reactor Safety (NRS) analysis to describe safety–relevant phenomena occurring in the reactor coolant system in greater detail. In this paper, the work about single-phase CFD simulation of rod bundles conducted in Shanghai Nuclear Engineering Research & Design Institute (SNERDI) is introduced. A single-phase methodology based on commercial software STAR-CCM+ is developed to simulate the flow field and temperature distribution in fuel rod bundles. Solid model is simply introduced at first. Mesh types, including tetrahedral, polyhedral and trimmer, are compared in order to select the most best one with both good accuracy and less cost. Several turbulence models available in STAR-CCM+, including standard k-epsilon model, realizable k-epsilon model (RKE), shear stress transport k-omega model (SST k-omega), and Reynolds stress model (RSM) are investigated. Trimmed mesh and RKE turbulence model with two-layer all y+ model are finally employed for following calculations. Vortex structures downstream of mixing vanes is qualitatively compared with Particle Image Velocity (PIV) results, and good agreement is achieved. The present method will be further refined in order to play significant role in future optimal design of fuel assembly (FA) grid.


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