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Extensional flow of polymer solutions through porous media
Authors:Saad Abdel-Aziz Ghoniem
Institution:(1) Dept. of Min., Pet., and Met. Engg., Faculty of Engineering, Cairo University, Giza, Egypt;(2) Reservoirs Department, K.O.C., Ahmadi-24, Kuwait
Abstract:The flow behaviour of various polymer solutions of non-hydrolyzed polyacrylamide, hydrolyzed polyacrylamide, polyox and Xanthan was investigated in a plexiglass column having a succession of enlargements and constrictions, and compared with the flow behaviour and mechanical degradation of a solution of non-hydrolyzed polyacrylamide in a packed column of non-consolidated sand. The flow behaviour of this solution was found to be very similar in both the sand pack and plexiglass pore.Apart from the Xanthan solution, all other polymer solutions showed a viscoelastic behaviour in the plexiglass pore. The onset of viscoelastic behaviour, which has previously been defined using the shear rate ( 
$$\dot \gamma $$
), stretch rate ( 
$$\dot \gamma $$
s ) and Ellis number (E 1), could be more precisely evaluated using a modified stretch rate (S G). The pressure losses across the plexiglass pore for different polymer solutions of the same type were found to follow a unique curve provided the suggested group (S G) was used, a situation which was not achieved with the other rheological parameters.The multipass mechanical degradation of the non-hydrolized polyacrylamide was tested through the sand pack against the suggested group (S G) and Maerker's group (M a). It was found that the loss of the solution viscoelasticity due to multipass mechanical degradation was better represented usingS G thanM a. A cross-sectional area (cm2) - C * critical concentration of polymer (ppm) - d plexiglass pore enlargement diameter - D average sand grain diameter (cm) - e equivalent width for the plexiglass pore - E 1 Ellis number (a Deborah number) - F R resistance factor - F Ri resistance factor at the first pass - h height of the flow path of the plexiglass pore - K power-law constant - K h,K w effective permeability to hydrocarbon and water, respectively (10–8 cm2) - M a Maerker's group for a given porosity (s–1) - M ai value ofM a at the first pass - N D Deborah number - n power-law index - Q flow rate (cm3/s) - R capillary radius (cm) - R g radius of gyration - S G suggested group of rheological parameters representing a modified maximum stretch rate (s–1) - S Gi value ofS G at the first pass - T R,t characteristic time for the fluid (s) - t s residence time (s) - V 0 superficial velocity (cm/s) - V mean velocity of flow through a porous medium (cm/s) - 
$$\bar V$$
average axial velocity in the enlargement section of the plexiglass pore (cm/s) - V 1,V 2 maximum velocity at a plexiglass enlargement neck and centre - eegr] intrincis viscosity - eegr viscosity (mPa s) - eegr r relative viscosity (ratio of the viscosity of the polymer solution to that of the solvent) - 
$$\dot \gamma $$
shear rate (s–1) - 
$$\dot \gamma $$
s stretch rate (s–1) - theta characteristic time for the polymer solution (s)
Keywords:Extensional flow  porous medium  polymer solution  viscoelasticity  degradation
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