Pressure Losses and Limiting Reynolds Numbers for Non-Newtonian Fluids in Short Square-Edged Orifice Plates

Author:

Ntamba Ntamba Butteur1,Fester Veruscha1

Affiliation:

1. Faculty of Engineering, Cape Peninsula University of Technology, P.O. Box 652, Cape Town, 8000, South Africa

Abstract

Correlations predicting the pressure loss coefficient along with the laminar, transitional, and turbulent limiting Reynolds numbers with the β ratio are presented for short square-edged orifice plates. The knowledge of pressure losses across orifices is a very important industrial problem while predicting pressure losses in piping systems. Similarly, it is important to define stable operating regions for the application of a short orifice at lower Reynolds numbers. This work experimentally determined pressure loss coefficients for square-edged orifices for orifice-to-diameter ratios of β = 0.2, 0.3, 0.57, and 0.7 for Newtonian and non-Newtonian fluids in both laminar and turbulent flow regimes.

Publisher

ASME International

Subject

Mechanical Engineering

Reference33 articles.

1. Flow Through Pipe Orifices at Low Reynolds Numbers;Johansen;Proc. R. Soc. London, Ser. A

2. Investigation of the Discharge and Coefficients of Small Circular Orifices;Medaugh;Civil Engineering

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4. Critical Reynolds Number for Orifice and Nozzle Flows in Pipes;Lakshmana Rao;J. Hydraul. Res.

5. Friction Losses in Valves and Fittings for Viscoplastic Fluids;Telis-Romero;Can. J. Chem. Eng.

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