Please use this identifier to cite or link to this item:
http://hdl.handle.net/11189/5689
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Ntamba-Ntamba, BM | en_US |
dc.contributor.author | Fester, Veruscha G | en_US |
dc.date.accessioned | 2017-06-12T09:21:54Z | - |
dc.date.available | 2017-06-12T09:21:54Z | - |
dc.date.issued | 2012 | - |
dc.identifier.citation | Journal of Fluids Engineering-Transactions of the ASME, 134:091204-1-091204-9, 2012 | en_US |
dc.identifier.uri | http://dx.doi.org/10.1115/1.4007156 | - |
dc.identifier.uri | http://hdl.handle.net/11189/5689 | - |
dc.description.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 ββ = 0.2, 0.3, 0.57, and 0.7 for Newtonian and non-Newtonian fluids in both laminar and turbulent flow regimes. | en_US |
dc.language.iso | en | en_US |
dc.publisher | Journal of Fluids Engineering | en_US |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-sa/3.0/za/ | - |
dc.subject | Pressure Losses | en_US |
dc.subject | Reynolds numbers | en_US |
dc.subject | Non-Newtonian Fluids | en_US |
dc.subject | Short square-edged orifice plates | en_US |
dc.title | Pressure losses and limiting Reynolds number for non-Newtonian fluids in short square-edged orifice plates | en_US |
dc.type.patent | Article | en_US |
Appears in Collections: | Eng - Journal articles (DHET subsidised) |
This item is licensed under a Creative Commons License