4,953 research outputs found
Measurements of the Solid-body Rotation of Anisotropic Particles in 3D Turbulence
We introduce a new method to measure Lagrangian vorticity and the rotational
dynamics of anisotropic particles in a turbulent fluid flow. We use 3D printing
technology to fabricate crosses (two perpendicular rods) and jacks (three
mutually perpendicular rods). Time-resolved measurements of their orientation
and solid-body rotation rate are obtained from stereoscopic video images of
their motion in a turbulent flow between oscillating grids with
=. The advected particles have a largest dimension of 6 times
the Kolmogorov length, making them a good approximation to anisotropic tracer
particles. Crosses rotate like disks and jacks rotate like spheres, so these
measurements, combined with previous measurements of tracer rods, allow
experimental study of ellipsoids across the full range of aspect ratios. The
measured mean square tumbling rate, ,
confirms previous direct numerical simulations that indicate that disks tumble
much more rapidly than rods. Measurements of the alignment of crosses with the
direction of the solid-body rotation rate vector provide the first direct
observation of the alignment of anisotropic particles by the velocity gradients
of the flow.Comment: 15 pages, 7 figure
κ΄μ±μ μμ μΉ¨ κ°μλμ λλ₯κ° λ―ΈμΉλ μν₯μ λν μ€νμ°κ΅¬
νμλ
Όλ¬Έ(μμ¬) -- μμΈλνκ΅λνμ : 곡과λν 건μ€ν경곡νλΆ, 2023. 2. λ°μ©μ±.Existing particle tracking models predict the vertical velocity of particles using the linear summation of carrier fluid velocity, the settling velocity in still fluid, and the random value following normal distribution to represent the effect of diffusion and dispersion. However, it has been reported that the terminal settling velocity of inertial particles changed in a turbulent flow. Therefore, it is necessary to investigate the interactions between advection by carrier fluid, settling velocity in stagnant water, and changes of settling velocity in a turbulent flow to improve the performance of predicting particle transport in particle tracking models. To this end, numerical simulations and laboratory experiments were conducted in the present study. First of all, the numerical simulations for the particle settlement in a steady uniform flow have been carried out to evaluate the effect of a parallel advection on the settling velocity. The resultant settling velocity was the same as the velocity calculated by superposing the advection by carrier fluid and the settling velocity in still fluid because the particles relative velocity has to be consistent according to the particle and fluid characteristics. To investigate the turbulence effect on the settling velocity, two kinds of experiments, namely, the open-channel flow experiments and experiments using the Vertical Recirculation Tube (VeRT), were conducted. In both of the experiments, the velocity of inertial particles was measured using particle tracking velocimetry (PTV), and fluid velocity and turbulence were measured using particle image velocimetry (PIV). In the present study, the PTV algorithm, which can track multiple settling particles, has been constructed. The experimental results showed that the settling velocity of the particles was generally larger in turbulent flow than in stagnant water. Then, several parameters representing particle and turbulence characteristics, such as Stokes number (St) and Rouse number (Sv) were investigated to determine which parameter depends on settling velocity change. As a result, the combination of Stokes and Rouse number, SvSt, which can be seen as a length scale parameter, appears to show a more evident correlation with the settling velocity change than other parameters. Thus, it is maintained that SvSt can be used as a defining parameter to describe the turbulence effect on the settling velocity change of inertial particles in a turbulent flow.
In conclusion, through the experiments conducted in the present study and preceding studies, it was evident that the settling velocity generally increases with increasing level of turbulence. Hence, the existing particle tracking model could overestimate the transport distance, which is mainly determined by the ratio of the settling distance to vertical velocity of particles. Thus, it is important to take into account the turbulence effect on the settling velocity of inertial particles in order to improve the performance of particle transport.κΈ°μ‘΄μ μ
μμΆμ λͺ¨λΈμ μ£Όλ³ μ 체μ μ μκ³Ό μ
μμ μ μ§ μ체μμμ μΉ¨κ°μλ κ·Έλ¦¬κ³ λΆμ°κ³Ό νμ° ν¨κ³Όλ₯Ό λνλ΄κΈ° μν΄ μ κ· λΆν¬λ₯Ό λ°λ₯΄λ μμ κ°μ μ ν ν©μΌλ‘ μ
μμ μ°μ§ λ°©ν₯ μλλ₯Ό μμΈ‘νλ€. νμ§λ§ λ§μ μ ν μ°κ΅¬λ€μ λλ₯ νλ¦μμ μ
μμ μ΅μ’
μΉ¨κ°μλκ° λ³νλ€λ κ²μ μ μν΄μλ€. λ°λΌμ μ
μμΆμ λͺ¨λΈμ μ
μ μμ‘(particle transport)μ λν μ νλ ν₯μμ μν΄, μ£Όλ³ μ 체μ μν μ΄μ‘(advection), μ μ§ μ체μμμ μ
μ μΉ¨κ°μλ, κ·Έλ¦¬κ³ λλ₯ νλ¦μμμ μΉ¨κ°μλ λ³ν κ°μ μνΈμμ©μ λν΄ μ‘°μ¬ν νμκ° μλ€. μ΄λ₯Ό μν΄, λ³Έ μ°κ΅¬μμλ μμΉ λͺ¨μμ μ€νμ€ μ€νμ΄ μνλμλ€. λ¨Όμ , μ
μμ μΉ¨κ° λ°©ν₯κ³Ό ννν μ΄μ‘μ΄ μμ©ν λ μΉ¨κ°μλμ λ―ΈμΉλ μν₯μ νκ°νκΈ° μν΄, μ μλ₯μμ μ
μμ μΉ¨κ° κ±°λμ λν μμΉ λͺ¨μκ° μνλμλ€. κ·Έ κ²°κ³Ό, μ΄μ‘μ μν₯μ λ°μ μΉ¨κ° μλλ μ μ§ μ체μμμ μΉ¨κ°μλμ μ£Όλ³ μ 체μ μ μμ μ€μ²©μ ν΅ν΄ κ³μ°λ κ²κ³Ό κ°μμΌλ©°, μ΄λ μ 체 λ΄μ κ΄μ±μ
μμ κ±°λμ λν μ΄λλ°©μ μμ ν΅ν΄, μ 체μ λν μ
μμ μλμλκ° μ
μ 쑰건μ λ°λΌ μΌμ νκΈ° λλ¬Έμμ νμΈνμλ€. λ€μμΌλ‘, μΉ¨κ° μλμ λλ₯κ° λ―ΈμΉλ μν₯μ μ‘°μ¬νκΈ° μν΄ μ
μμ μΉ¨κ°κ³Ό μμ§ λ°©ν₯μΌλ‘ μ μ²΄κ° μ΄λνλ κ°μλ‘ νλ¦μμμ μ€νκ³Ό μΉ¨κ°κ³Ό ννν λ°©ν₯μΌλ‘ μ μ²΄κ° μ΄λνλ μ°μ§μνμλ‘(Vertical Recirculation Tube; VeRT) μ€νμ μ§ννμλ€. λ κ°μ§ μ€νμμ, μ€ν μ
μμ μλλ PTV(Particle Tracking Velocimetry) κΈ°λ²μ ν΅ν΄ μΈ‘μ λμμΌλ©°, μ 체μ μλμ λλ₯λ PIV(Particle Image Velocimetry) κΈ°λ²μ ν΅ν΄ μΈ‘μ λμλ€. νΉν, λ³Έ μ°κ΅¬μμλ μ¬λ¬ κ°μ μ
μλ₯Ό ν¨κ» μΆμ κ°λ₯ν PTV μκ³ λ¦¬μ¦μ ꡬμΆνμ¬ μ¬μ©νμλ€. μ€ν κ²°κ³Όλ μ
μμ μΉ¨κ°μλκ° μΌλ°μ μΌλ‘ μ μ§ μμ²΄λ³΄λ€ λλ₯ νλ¦μμ λ λΉ λ₯΄λ€λ κ²μ 보μ¬μ£Όμκ³ , κ·Έ μΉ¨κ°μλ λ³νμ μ΄λ€ μΈμκ° μ’
μμ μΈμ§λ₯Ό Stokes μ, Rouse μ λ± μ
μ λ° λλ₯ νΉμ±μ ν¨κ» λνλ΄λ λͺ κ°μ§ μΈμλ€μ λμμΌλ‘ μ‘°μ¬νμλ€. κ·Έ κ²°κ³Ό, Stokes μμ Rouse μλ₯Ό κ³±νμ¬ μ
μμ λλ₯ νΉμ±μ κΈΈμ΄ μ°¨μ λΉλ₯Ό λνλ΄λ κ° ν΄λΉ κ°μ΄ μ¦κ°ν¨μ λ°λΌ μΉ¨κ° μλ λ³νμ¨μ΄ κ°μνλ ννλ₯Ό λ€λ₯Έ μΈμλ€μ λΉν΄ λͺ
ννκ² λ³΄μ¬μ£Όμλ€. λ°λΌμ κ° λλ₯ νλ¦μμ κ΄μ±μ
μμ μΉ¨κ°μλ λ³νμ λλ₯κ° λ―ΈμΉλ μν₯μ μ€λͺ
ν μ μλ κ°μ₯ μ§λ°°μ μΈ μΈμλ‘ μ¬μ©λ μ μμμ νμΈνμλ€.
κ²°λ‘ μ μΌλ‘, λ³Έ μ°κ΅¬μμ μνλ μ€νλ€κ³Ό μ ν μ°κ΅¬μ κ²°κ³Όλ‘λΆν° λλ₯ νλ¦μμ μΉ¨κ° μλλ λμ²΄λ‘ μ¦κ°ν¨μ κ΄μΈ‘νμλ€. λ°λΌμ κΈ°μ‘΄μ μ
μμΆμ λͺ¨λΈμ μ
μμ μ°μ§λ°©ν₯ μ μμ κ³Όμμ°μ ν μ μμΌλ©°, μ΄μ λ°λΌ μ
μμ μμ‘ κ±°λ¦¬λ₯Ό κ³Όλμ°μ ν μ μλ€. κ·Έλ¬λ―λ‘, νΉμ ν μ
μ λ° νλ¦ μ‘°κ±΄μμ μΉ¨κ° μλμ λ³νλ₯Ό μμΈ‘ν μ μλλ‘ μΆκ°μ μΈ μ°κ΅¬λ₯Ό μννκ³ , μ΄λ₯Ό μ
μμΆμ λͺ¨λΈμ μ νλ ν₯μμ μν΄ μ
μ κ±°λ ν΄μμ λ°μν νμκ° μλ€.1. Introduction 1
1.1 Background and necessities of study 1
1.2 Research objectives 3
2. Theoretical background 7
2.1 Inertial particles in a viscous fluid 7
2.1.1 Equation of motion 7
2.1.2 Numerical integration scheme for the MRE 12
2.2 Settling velocity of inertial particles 16
2.2.1 Terminal settling velocities in Stokes regime 16
2.2.2 Settling velocity changes in turbulence 17
2.3 Estimating turbulent kinetic energy (TKE) dissipation rate for turbulence analysis 22
2.3.1 Particle Image Velocimetry (PIV) 22
2.3.2 TKE dissipation rate 22
2.3.3 The method estimating TKE dissipation rate from PIV data suggested by Sheng et al. (2000) 25
2.4 Empirical Mode Decomposition (EMD) 32
3. Experimental setup and instrumentations 34
3.1 Experimental setup 34
3.1.1 Experiment 1: Open-channel flume 34
3.1.2 Experiment 2: Vertical Recirculation Tube (VeRT) 44
3.2 Particle Tracking Velocimetry (PTV) 57
4. Results and discussion 63
4.1 Effect of parallel advection on the settling velocity 63
4.1.1 Modified drag force in MRE 63
4.1.2 Validation of the numerical scheme 65
4.1.3 Numerical simulation in a steady uniform flow 70
4.2 Experimental results 73
4.2.1 Experiment 1: Open-channel flume 73
4.2.2 Experiment 2: VeRT 88
4.3 Effect of turbulence on settling velocity change 101
5. Conclusion 113
REFERENCES 116
APPENDIX 121
κ΅λ¬Έμ΄λ‘ 131μ
Turbulent channel flow of dense suspensions of neutrally-buoyant spheres
Dense particle suspensions are widely encountered in many applications and in
environmental flows. While many previous studies investigate their rheological
properties in laminar flows, little is known on the behaviour of these
suspensions in the turbulent/inertial regime. The present study aims to fill
this gap by investigating the turbulent flow of a Newtonian fluid laden with
solid neutrally-buoyant spheres at relatively high volume fractions in a plane
channel. Direct Numerical Simulation are performed in the range of volume
fractions Phi=0-0.2 with an Immersed Boundary Method used to account for the
dispersed phase. The results show that the mean velocity profiles are
significantly altered by the presence of a solid phase with a decrease of the
von Karman constant in the log-law. The overall drag is found to increase with
the volume fraction, more than one would expect just considering the increase
of the system viscosity due to the presence of the particles. At the highest
volume fraction here investigated, Phi=0.2, the velocity fluctuation
intensities and the Reynolds shear stress are found to decrease. The analysis
of the mean momentum balance shows that the particle-induced stresses govern
the dynamics at high Phi and are the main responsible of the overall drag
increase. In the dense limit, we therefore find a decrease of the turbulence
activity and a growth of the particle induced stress, where the latter
dominates for the Reynolds numbers considered here.Comment: Journal of Fluid Mechanics, 201
Accurate direct numerical simulation of two-way coupled particle-laden flows through the nonuniform fast Fourier transform
The ability of the non-uniform Fast Fourier Transform (NUFFT) to predict the particle feedback on the flow in particle-laden flows in the two-way coupling regime is examined. In this regime, the particle back-reaction on the fluid phase can substantially modify the flow statistics across all the scales, when particle loading is significant. While many works in the literature focus on the direct B-spline interpolation, which is now a well-established method for the one-way coupling, only a few methods are available for the computation of particle back-reaction, which are often lower order and reduce the overall accuracy of the simulation. In our implementation, particle momentum and temperature back-reactions on the fluid flow are computed by means of the forward NUFFT with B-spline basis, while the B-spline interpolation is performed as a backward NUFFT. An application of the NUFFT to the simulation of a statistically steady and isotropic turbulent flow, laden with inertial particles is presented. The effect of particle feedback on velocity and temperature structure functions and on particle clustering is discussed as a function of the Stokes number, together with the spectral characterization of the particle phase
Bias in particle tracking acceleration measurement
We investigate sources of error in acceleration statistics from Lagrangian
Particle Tracking (LPT) data and demonstrate techniques to eliminate or
minimise bias errors introduced during processing. Numerical simulations of
particle tracking experiments in isotropic turbulence show that the main
sources of bias error arise from noise due to position uncertainty and
selection biases introduced during numerical differentiation. We outline the
use of independent measurements and filtering schemes to eliminate these
biases. Moreover, we test the validity of our approach in estimating the
statistical moments and probability densities of the Lagrangian acceleration.
Finally, we apply these techniques to experimental particle tracking data and
demonstrate their validity in practice with comparisons to available data from
literature. The general approach, which is not limited to acceleration
statistics, can be applied with as few as two cameras and permits a substantial
reduction in the spatial resolution and sampling rate required to adequately
measure statistics of Lagrangian acceleration
- β¦