Predicting laminar-turbulent transition in Poiseuille pipe flow for non-Newtonian fluids

Güzel B., Frigaard I., Martinez D.

Chemical Engineering Science, cilt.64, sa.2, ss.254-264, 2009 (SCI-Expanded, Scopus) identifier

  • Yayın Türü: Makale / Tam Makale
  • Cilt numarası: 64 Sayı: 2
  • Basım Tarihi: 2009
  • Doi Numarası: 10.1016/j.ces.2008.10.011
  • Dergi Adı: Chemical Engineering Science
  • Derginin Tarandığı İndeksler: Science Citation Index Expanded (SCI-EXPANDED), Scopus
  • Sayfa Sayıları: ss.254-264
  • Anahtar Kelimeler: Non-Newtonian fluids, Pipe flow, Turbulent transition, Yield stress
  • İstanbul Gelişim Üniversitesi Adresli: Hayır

Özet

We present a new phenomenological approach for quantifying laminar-turbulent transition in pipe flow. This criterion is based on averaging a local Reynolds number to give ReG. Our localised parameter shows strong radial variations that are maximal at approximately the radial positions where puffs first appear during the first stages of turbulent transition. We present comparative data for experiments conducted with Glycerin, Xanthan and Carbopol solutions, each of which serves to demonstrate the validity of our approach. Crown Copyright © 2008.