Skip to main content
Log in

Particle mixing and diffusion in the turbulent wake of cylinder arrays

  • Originals
  • Published:
Experiments in Fluids Aims and scope Submit manuscript

Abstract

The collection of 10 μ DOP droplets from an aerosol flow around an array of five circular cylinders in a turbulent air stream was measured. Axial and angled alignments of the target array, normal to the flow, were examined. Cylinder Reynolds numbers ranged from 1,300 to 5,100, and effective Stokes numbers from 0.50 to 1.58. A continuous line source turbulent diffusion model was used with the centerline velocity and concentration distributions to derive the eddy diffusion coefficients for momentum and particle concentration in the near wake of the cyinders. Angled collection results showed an optimal target alignment at the edge of the momentum wake of the lead cylinder. Further examination with an LDA system suggests the peak in collection is due to a particle velocity surplus in the wake.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

Abbreviations

A k :

projected area of cylinder k

A t :

cross sectional area of flow

b :

wake width

C :

particle concentration

C 1 :

concentration deficit

C D.n :

drag coefficient of nth cylinder

d :

diameter

φ :

vortex shedding frequency

L c :

length of cylinder

n :

cylinder rank

Q :

strength of line source

R L :

Lagrangian time autocorrelation coefficient

Re :

Reynolds number (U dρ/μ)

T L :

Lagrangian integral time scale

U :

x-directed velocity

U 1 :

velocity deficit

u :

fluctuating axial velocity component

v :

fluctuating lateral velocity component

V :

drop volume

x :

intercylinder spacing

y :

lateral displacement

β :

mixing length proportionality constant

A :

measured droplet diameter

ɛ :

eddy diffusivity

η * :

corrected collection efficiency

θ :

contact angle of droplet on surface

μ :

viscosity of air

ρ :

density

τ :

time

Ψ :

non-Stokesian drag correction factor

c :

cylinder

g :

gas

M :

momentum

p :

particles

θ :

theoretical (Stokes efficiency)

aneth:

freestream value

1, n :

cylinder rank 1 or n

References

  • Baldwin, L. V.; Walsh, T. J. 1961: Turbulent diffusion in the core of fully developed pipe flow. AIChE J. 7, 53–61

    Google Scholar 

  • Bokaian, A.; Geoola, F. 1984: Vortex shedding from two interfering circular cylinders. J. Eng. mech. 110, 623–628

    Google Scholar 

  • Burkholtz, A. 1978: Aerosol separation on cylinders exposed to flow-comparison of measured and theoretical data. J. Aerosol Sci. 9, 199–207

    Google Scholar 

  • Cantwell, B.; Coles, D. 1983: An experimental study of entrainment and transport in the turbulent near wake of a circular cylinder. J. Fluid mech. 136, 321–374

    Google Scholar 

  • Choudhary, K. R.; Gentry, J. W. 1977: A model for particle collection with potential flow between two parallel cylinders. Can. J. Chem. Eng. 55, 403–407

    Google Scholar 

  • Douglas, P. L. 1980: The deposition of aerosols on cylinders in turbulent cross flow. Ph.D Thesis, Univ. Waterloo, Waterloo Ontario

    Google Scholar 

  • Dryden, H. L. 1939: Turbulence and diffusion. 1 & EC 31, 416–425

    Google Scholar 

  • Fenton, D. L.; Stukel, J. J. 1976: Flow of a particulate suspension in the Wake of a circular cylinder. Int. J. Multiphase Flow 3, 123–139

    Google Scholar 

  • Fleischman, S. T.; Sallet, D. W. 1981: Vortex shedding from cylinders and the resulting unsteady flow phenomena. Shock and Vibration Digest 13, 9–22

    Google Scholar 

  • Frenkiel, F. N. 1950: Institute for fluid dynamics and applied mathematids. Lecture Series No. 3, Univ. Maryland, College Park MD

    Google Scholar 

  • Good, J. R.; Stromberg, R. R. 1979: Surface and colloid science, Vol. II, Experimental Methods. New York: Plenum Press

    Google Scholar 

  • Hinze, J. O. 1975: Turbulence. New York: McGraw Hill

    Google Scholar 

  • Israel, R.; Rosner, D. E. 1983: Use of a generalized stokes number to determine the aerodynamic capture efficiency of non-stokesian particles for a compressible gas flow. Aerosol Sci. & Tech. 2, 45–51

    Google Scholar 

  • Jacober, D. E.; Matteson, M. J. 1986: The collection of aerosols from gas streams by impaction on multiple spherical targets. Aerosol Sci. & Tech. 4, 433–443

    Google Scholar 

  • Langmuir, J.; Blodgett, K. B. 1946: US Army Tech. Rep. 5418

  • Ranz, W. E.; Wong, J. B. 1952: Impaction of smoke and dust particles on surface and body collectors. I & EC 44, 1371–1380

    Google Scholar 

  • Schlichting, H. 1979: Boundary layer theory. New York: McGraw Hill

    Google Scholar 

  • Sherwood, T. K.; Pigford, R. L.; Wilke, C. R. 1975: Mass transfer. New York: McGraw Hill

    Google Scholar 

  • Uberoi, M. S.; Corrsin, S. 1952: NACA Tech. Note 2710

  • Zdravkovich, M. M. 1977: Review of flow interference between two circular cylinders in various arrangements. ASME J. Fluids Eng. 99, 618–633

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Helgesen, J.K., Matteson, M.J. Particle mixing and diffusion in the turbulent wake of cylinder arrays. Experiments in Fluids 10, 333–340 (1991). https://doi.org/10.1007/BF00190249

Download citation

  • Received:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF00190249

Keywords

Navigation