US 12,135,266 B2
Real time monitoring of non-Newtonian fluids
Dwayne E. McDaniel, Miami, FL (US); Ahmadreza Abbasi Baharanchi, Miami, FL (US); Michael Poirier, Aiken, SC (US); and Shervin Tashakori, Miami, FL (US)
Assigned to The Florida International University Board of Trustees, Miami, FL (US); and Savannah River Nuclear Solutions, LLC, Aiken, SC (US)
Filed by The Florida International University Board of Trustees, Miami, FL (US); and Savannah River Nuclear Solutions, LLC, Aiken, SC (US)
Filed on Mar. 8, 2022, as Appl. No. 17/654,006.
Claims priority of provisional application 63/158,060, filed on Mar. 8, 2021.
Prior Publication US 2022/0291106 A1, Sep. 15, 2022
Int. Cl. G01N 11/08 (2006.01); G01N 11/00 (2006.01)
CPC G01N 11/08 (2013.01) [G01N 2011/0033 (2013.01)] 4 Claims
OG exemplary drawing
 
1. A system for determining yield stress of a non-Newtonian fluid, the system comprising:
a pipe containing the non-Newtonian fluid;
a differential type pressure transmitter connected to a first point of the pipe and a second point of the pipe, the pipe containing therein a fully-developed laminar flow of the non-Newtonian fluid between the first point and the second point;
a processor;
a machine-readable medium in operable communication with the processor and having instructions stored thereon that, when executed by the processor, solve equations (1), (2), and (3) in order to determine the yield stress of the non-Newtonian fluid; and
a flow meter connected to the pipe and configured to measure a velocity of the non-Newtonian fluid,
the differential type pressure transmitter being configured to measure a first pressure of the pipe at the first point and a second pressure of the pipe at the second point,
the yield stress of the non-Newtonian fluid being determined in real time by the processor using the difference between the first pressure and the second pressure as an input to equation (1), and
equations (1), (2), and (3) being as follows

OG Complex Work Unit Math
where ΔP is the difference between the first pressure and the second pressure, L is a predetermined length of the pipe between the first point and the second point, D is a predetermined diameter of the pipe between the first point and the second point, o is a predetermined density of the non-Newtonian fluid, f is a frictional coefficient of the non-Newtonian fluid, V is the velocity of the non-Newtonian fluid in the pipe between the first point and the second point measured by the flow meter, μ is a viscosity of the non-Newtonian fluid, Re is a Reynolds number of the non-Newtonian fluid in the pipe between the first point and the second point, He is a Hedstrom number of the non-Newtonian fluid in the pipe between the first point and the second point, and ty is the yield stress of the non-Newtonian fluid.