Skip to main content
Log in

Sedimentation of particles in shear flows of viscoelastic fluids with fibers

  • Original Contribution
  • Published:
Rheologica Acta Aims and scope Submit manuscript

Abstract

We study the effect of fiber additives on rheology and sedimentation of particle suspensions in a base viscoelastic suspending fluid in the case when the suspension is subjected to shear flow. We found experimentally that fiber additives (3–6 mm in length and 8–12 μm in diameter at a mass fraction of 0–0.4%) increase the suspension viscosity and retard the particle sedimentation significantly. At the same mass concentration, long and thin fibers reduce the sedimentation velocity and increase the viscosity to a much greater extent than short and thick fibers. We revealed that both rheology and sedimentation are controlled by a single conformational parameter (overlap parameter) defined as the number of fibers per unit volume multiplied by fiber length cubed.

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.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8

Similar content being viewed by others

Notes

  1. The standard way of defining the best fit is to choose the parameters so that the sum of the squares of the deviations of the theoretical curve(s) from the experimental points for a range of independent variables: \( {x}^2\left({p}_1,{p}_2,\dots \right)=\frac{1}{n^{eff}-p}\sum_i\sum_j{w}_{ji}{\left[{y}_{ji}-{f}_j\left({x}_{1i},{x}_{2i}\dots; {p}_1,{p}_2,\dots \right)\right]}^2 \)

    is at its minimum. Here, y ji are the measured values of the dependent (output) variable y j for the values of the independent (input) variables x 1 = x 1i  , x 2 = x 2i  , … ; n eff is the total number of experimental points used in the fitting, and p is the total number of adjustable parameters used in the fitting (the difference d = n eff − p is usually referred to as the number of degrees of freedom).

    The quantities w ji represent the weights of each experimental point. Instrumental weights: \( {w}_{ji}=1/{\sigma}_{ji}^2 \) , where σ ji are the errors of the measurement. (From the Help of Origin graphics software package)

References

  • Barnes HA, Hutton JF, Walters K (1989) An introduction to rheology. Elsevier, Amsterdam

    Google Scholar 

  • Bazilevskii AV, Rozhkov AN (2009) Motion of a sphere down an inclined plane in a viscous flow. Fluid Dyn 44(4):566–576

    Article  Google Scholar 

  • Bazilevskii AV, Koroteev DA, Rozhkov AN, Skobeleva AA (2010) Sedimentation of particles in shear flows of viscoelastic fluids. Fluid Dyn 45(4):626–637

    Article  Google Scholar 

  • Bazilevsky AV, Kalinichenko VA, Plyashkevich VA, Badazhkov DV, Rozhkov AN (2016a) Sedimentation of particles in shear flows of fluids with fibers. Rheol Acta 55(1):11–22

    Article  Google Scholar 

  • Bazilevsky AV, Kalinichenko VA, Plyashkevich VA, Badazhkov DV, Rozhkov AN (2016b) Sedimentation of particles in shear flows of viscoelastic fluids with fibers. Preprint IPMech RAS № 1127., Moscow

  • Dogon D, Golombok M (2016a) Flow-induced proppant carrying capacity. J Pet Sci Eng 146:308–317

    Article  Google Scholar 

  • Dogon D, Golombok M (2016b) Self-regulating solutions for proppant transport. Chem Eng Sci 148:219–228

    Article  Google Scholar 

  • Elgaddafi R, Ahmed R, George M, Growcock F (2012) Settling behavior of spherical particles in fiber-containing drilling fluids. J Pet Sci Eng 84-85:20–28

    Article  Google Scholar 

  • Gheissary G, van der Brule BHAA (1996) Unexpected phenomena observed in particle settling in non-Newtonian media. J Non-Newtonian Fluid Mech 67(1):1–18

    Article  Google Scholar 

  • Harlen OG, Sundararajakumar RR, Koch DL (1999) Numerical simulations of a sphere settling through a suspension of neutrally buoyant fibers. J Fluid Mech 388:355–388

    Article  Google Scholar 

  • Hinch EJ (1977) Mechanical models of dilute polymer solutions in strong flows. Phys Fluids 20(10 Pt 2):S22–S30

    Article  Google Scholar 

  • Liu Y, Sharma MM (2005) Effect of fracture width and fluid rheology on proppant settling and retardation: an experimental study. SPE/DOE 96208:1–12

    Google Scholar 

  • Osiptsov AA (2017) Fluid mechanics of hydraulic fracturing: a review. J Pet Sci Eng 156:513–535

    Article  Google Scholar 

  • Roodhart LP (1985) Proppant settling in non-Newtonian fracturing fluids. SPE/DOE 13905:1–10

    Google Scholar 

  • Shalagina AE, Fu D (2015) Treatment fluid. Patent WO 2015160275 A1

  • Shalagina AE, Kraemer C, Inozemtseva EA (2015) Fluide de traitement. Patent WO 2015160277–A1

  • Taylor JR (1997) An introduction to error analysis: the study of uncertainties in physical measurements. University Science, Sausalito

    Google Scholar 

Download references

Acknowledgments

The study was conducted under Research Contract No. Slb-FAC-24/01/2014-IPM_RAN/TCS between Schlumberger Technology Corporation and the Ishlinsky Institute for Problems in Mechanics, Russian Academy of Sciences. The authors thank Professor R.V. Goldstein for his help throughout the work. The final preparation of the paper was supported by the Russian Foundation for Basic Research (Grant No. 15-08-01365).

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Aleksey N. Rozhkov.

Electronic supplementary material

ESM 1

(DOCX 12847 kb)

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Bazilevsky, A.V., Kalinichenko, V.A., Plyashkevich, V.A. et al. Sedimentation of particles in shear flows of viscoelastic fluids with fibers. Rheol Acta 56, 787–799 (2017). https://doi.org/10.1007/s00397-017-1036-x

Download citation

  • Received:

  • Revised:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s00397-017-1036-x

Keywords

Navigation