DOCSLIB.ORG

Concentric Cylinder Viscometer Flows of Herschel-Bulkley Fluids Received Sep 09, 2019; Accepted Nov 28, 2019

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
Concentric Cylinder Viscometer Flows of Herschel-Bulkley Fluids Received Sep 09, 2019; Accepted Nov 28, 2019 Appl. Rheol. 2019; 29 (1):173–181 Research Article Hans Joakim Skadsem* and Arild Saasen Concentric cylinder viscometer flows of Herschel-Bulkley fluids https://doi.org/10.1515/arh-2019-0015 Received Sep 09, 2019; accepted Nov 28, 2019 Abstract: Drilling fluids and well cements are example τ non-Newtonian fluids that are used for geothermal and Cement slurry petroleum well construction. Measurement of the non- Spacer Newtonian fluid viscosities are normally performed using a concentric cylinder Couette geometry, where one of the Shear stress, Drilling fluid cylinders rotates at a controlled speed or under a con- trolled torque. In this paper we address Couette flow of yield stress shear thinning fluids in concentric cylinder geometries. We focus Chemical wash on typical oilfield viscometers and discuss effects of yield Shear rate,γ ˙ stress and shear thinning on fluid yielding at low viscome- ter rotational speeds and errors caused by the Newtonian Figure 1: Example of typical flow curves for fluids involved in well shear rate assumption. We relate these errors to possible construction. implications for typical wellbore flows. Keywords: Drilling fluids, Herschel-Bulkley, Viscometry The operation schedule involves drilling, where the drilling fluid transports out drilled cuttings, displacement PACS: 83.85.Jn, 83.60.La, 83.10.Gr, 47.57.Qk of the drilling fluid from the narrow annular space be- tween the casing string and the formation and replace it by a cement slurry to create a total zonal isolation in the well. 1 Introduction Once in place, the cement slurry is allowed to harden into a cement sheath. A successful operation is dependent on the In the enterprise of constructing geothermal or petroleum complete displacement of drilling fluid from the narrow an- wells, drilling fluids and well cements are used. These nular space outside the casing. This is typically achieved fluids are constructed as a blend of particle suspensions, by injecting a sequence of wash and spacer fluids ahead liquid-liquid dispersions and polymer solutions with a of the cement slurry, and the displacement is optimized large variety of additional chemicals. The fluids show a through careful design of fluid densities and viscosities. As strong non-Newtonian characteristic. illustrated by the example flow curves in Figure 1, the in- As an example, in Figure 1 we plot typical shapes of volved fluids typically exhibit yield stress and thus show flow curves for fluids involved in the operation where acas- shear thinning behavior. Most drilling fluids, and some ce- ing string is cemented to the newly drilled formation. Pri- ments slurries also exhibit a curved shape of the viscosity mary cementing is performed once the current well section flow curve after reaching the yield stress; i.e. yield stress is drilled to target depth and a casing string is run into the shear thinning fluids as proposed by Herschel and Bulk- hole and to the bottom of the section. ley [1]. In addition to exhibiting shear thinning and yield stress behaviour, most drilling and well construction fluids are also thixotropic, i.e. requiring a certain time duration for microstructure equilibration to current shearing condi- tions [2, 3]. In this paper, we neglect thixotropic behaviour *Corresponding Author: Hans Joakim Skadsem: NORCE Nor- and instead focus on the steady state, non-Newtonian flow wegian Research Centre AS, Prof. Olav Hanssensvei 15, N-4021 curve of well construction fluids. Stavanger; Email: [email protected] Arild Saasen: University of Stavanger, N-4036 Stavanger Open Access. © 2019 H. J. Skadsem and A. Saasen, published by De Gruyter. This work is licensed under the Creative Commons Attribution 4.0 License 174 Ë H. J. Skadsem and A. Saasen Stable displacements are normally preferred for pri- For a concentric cylinder viscometer, Krieger and El- mary cementing operations in the laminar regime, imply- rod [7] showed that the angular velocity Ω of the rotating ing that the displacing fluid express a higher frictional cup is related to the shear rate and shear stress in the gap pressure loss than the drilling fluid to optimise displace- via Eq. (2) τ Z 1 ment. In practice this means that the cement should be 1 훾˙ (τ) Ω = dτ, (2) effectively more viscous than the fluid it displaces [4,5]. 2 τ 2 It is also essential to limit the circulating pressures in the κ τ1 well to avoid hydraulic fracturing the formation and un- where τ1 is again the wall shear stress at the inner bob and controlled loss of fluids. This means that to optimize dis- κ = R1/R2 is the ratio of bob to cup radii. As Ω is controlled placement and avoid formation fracturing during pump- and τ1 is measured, Eq. (2) is to be solved for the unknown ing, it is important to reduce the viscosity of the drilling shear rate 훾˙ (τ1). Krieger and Elrod [7] and later Krieger [8] fluids being in the annulus. However, this reduction can- showed that Eq. (2) can be solved for the unknown shear not be so large that the pressure control in the well is lost. rate via an infinite series without making a priori assump- Therefore, it is important to have accurate and reliable vis- tions of the type of flow curve for the fluid. These solutions cosity characterization of the fluids involved in the pro- do not always perform well for fluids with yield stresses [9] cesses. as yield stress introduces a mathematical singularity in the In the field, fluid viscosities are normally measured viscosity curve. Alternative solution strategies based on using a concentric cylinder Couette geometry, where the Tikhonov regularization [10, 11] and wavelet-vaguelette de- outer cup rotates at a fixed angular velocity Ω and the inner composition [12] have been developed, which are capable bob is held fixed by application of a torque M. The oilfield of handling yield stress fluids with no a priori flow curve standard for viscosity measurements are based on equip- assumption. ment description. The dimensions for the conventional oil- The problem of existence of yield stresses is sum- field viscometer were described by Savins and Roper [6]. marised by Watson [13]. However, for our purpose we con- The rotor-and-bob geometry is as follows: Rotor radius is sider sufficiently short time frames where use of an yield 1.8415 cm and the bob radius is 1.7247 cm. The length of stress is applicable. Therefore, as will be described later, the bob is 3.8 cm. These dimensions were partly sought to we will assume an existence of the yield stresses. present the viscosity at the shear rate of 511 s−1 directly in If the relationship between shear rate and shear stress units of centipoise and to allow for measurements of fluids is known a priori for the fluid in question, relations link- containing weighting particles of sizes less than 75 micron. ing angular velocity, applied torque and model parameters According to oilfield standards for well cementing, the vis- can be derived from Eq. (2), see e.g. Li et al.[14]. Following cometer should have at least the following rotation speeds: a different approach, Chatzimina et al.[15] solved the gov- 600, 300, 200, 100, 6 and 3 revolutions per minute (RPM). erning equations for Herschel-Bulkley fluids and found ex- The 600 RPM is used for drilling fluids and spacers, but not pressions for the wall shear rate in a concentric cylinder ge- for well cements as exposure to this shear rate reduces the ometry. They showed that wall shear rates may deviate sig- reproducibility of flow curves. Later, it has become anin- nificantly from corresponding Newtonian values depend- creasing use of viscometers with more rotation speeds in ing on the diameter ratio of the Couette geometry and ma- the oilfields. Typically, additional rotation speeds equal to terial parameters. 60, 30, 20, 10, 2, and 1 RPM can now occasionally be found In this paper, we assume a priori yield stress shear on oilfield equipment. The dimensions remain the same. thinning (Herschel-Bulkley) flow curves and study the ef- In the absence of end effects, the applied torque is re- fects of yield stress and shear thinning on the wall shear lated to the wall shear stress at the bob via rates. We compare the actual Herschel-Bulkley wall shear M rates to those of a Newtonian fluid and quantify the error in τ = , (1) 1 πR2L the common Newtonian assumption for model yield stress 2 1 fluids. The outline of the paper is as follows: Webegin where the submerged bob radius and length are denoted by considering the momentum equation for the Herschel- R1 and L, respectively. This results in a relationship be- Bulkley fluid in a Couette geometry in the next section. We tween angular velocity of the cup and the corresponding derive an equation relating rotational velocity of the cup shear stress at the bob surface. However, a relationship be- to the shear stress in the gap that is equivalent to what tween the shear rate and the corresponding shear stress is can be obtained through Eq. (2). Next we solve the gov- typically what is sought for. erning equation for azimuthal flow velocity in the gap and bob shear rate for a certain, fixed Herschel-Bulkley fluid. Concentric cylinder viscometer flows of Herschel-Bulkley fluids Ë 175 1000 Finally, we consider example Fann 35 model viscometer n =0.5 measurements of well construction fluids, including a typ- 100 n =0.75 n =1.0 ical water-based drilling fluid, a spacer fluid and cement 10 slurry, and investigate the difference between the Newto- actual 1 nian shear rate assumption and the non-Newtonian ) 0.1 wall shear rate.
Load more

Recommended publications
  • Couette and Planar Poiseuille Flow
    An Internet Book on Fluid Dynamics COUETTE AND PLANAR POISEUILLE FLOW Couette and planar Poiseuille flow are both steady flows between two infinitely long, parallel plates a fixed distance, h, apart as sketched in Figures 1 and 2. The difference is that in Couette flow one of the plates Figure 1: Couette flow. Figure 2: Planar Poiseuille flow. has a velocity U in its own plane (the other plate is at rest) as a result of the application of a shear stress, τ, and there is no pressure gradient in the fluid. In contrast in planar Poiseuille flow both plates are at rest and the flow is caused by a pressure gradient, dp/dx, in the direction, x, parallel to the plates. It is however, convenient, to begin the analysis of these flows together. We will omit any conservative body forces like gravity since their effects are can be simply added to the final solutions. Then, assuming that the only non-zero component of the velocity is ux and that the velocity and pressure are independent of time the resulting planar continuity equation for an incompressible fluid yields ∂ux ∂x =0 (Bib1) so that ux(y) is a function only of y, the coordinate perpendicular to the plates. Using this the planar Navier-Stokes equations for an incompressible fluid of constant and uniform viscosity reduce to 2 ∂p ∂ ux = μ (Bib2) ∂x ∂y2 ∂p ∂y =0 (Bib3) The second of these shows that the pressure, p(x), is a function only of x and hence the gradient, dp/dx, is well defined and a parameter of the problem.
    [Show full text]
  • Transition to Turbulence in Plane Poiseuille and Plane Couette Flow by STEVEN A
    J. Fluid Mech. (1980), vol. 96, part 1, pp. 159-205 169 Printed in Great Britain Transition to turbulence in plane Poiseuille and plane Couette flow By STEVEN A. ORSZAG AND LAWRENCE C. KELLST Department of Mathematics, Massachusetts Institute of Technology, Cambridge, MA 02139 [Received 8 June 1978 and in revised form 2 October 1978) Direct numerical solutions of the three-dimensional time-dependent Navier-Stokes equations are presented for the evolution of three-dimensional finite-amplitude disturbances of plane Poiseuille and plane Couette flows. Spectral methods using Fourier series and Chebyshev polynomial series are used. It is found that plane Poiseuille flow can sustain neutrally stable two-dimensional finite-amplitude dis- turbances at Reynolds numbers larger than about 2800. No neutrally stable two- dimensional finite-amplitude disturbances of plane Couette flow were found. Three-dimensional disturbances are shown to have a strongly destabilizing effect. It is shown that finite-amplitude disturbances can drive transition to turbulence in both plane Poiseuille flow and plane Couette flow at Reynolds numbers of order 1000. Details of the resulting flow fields are presented. It is also shown that plane Poiseuille flow cannot sustain turbulence at Reynolds numbers below about 500. I. Introduction One of the oldest unsolved problems of fluid mechanics is the theoretical description of the inception and growth of instabilities in laminar shear flows that lead to trans- ition to turbulence. The behaviour of small-amplitude disturbances on a laminar flow is reasonably well understood, but understanding of the behaviour of finite-amplitude disturbances is in a much less satisfactory state.
    [Show full text]
  • A Numerical and Experimental Investigation of Taylor Flow Instabilities in Narrow Gaps and Their Relationship to Turbulent Flow
    A NUMERICAL AND EXPERIMENTAL INVESTIGATION OF TAYLOR FLOW INSTABILITIES IN NARROW GAPS AND THEIR RELATIONSHIP TO TURBULENT FLOW IN BEARINGS A Dissertation Presented to The Graduate Faculty of The University of Akron In Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy Dingfeng Deng August, 2007 A NUMERICAL AND EXPERIMENTAL INVESTIGATION OF TAYLOR FLOW INSTABILITIES IN NARROW GAPS AND THEIR RELATIONSHIP TO TURBULENT FLOW IN BEARINGS Dingfeng Deng Dissertation Approved: Accepted: _______________________________ _______________________________ Advisor Department Chair Dr. M. J. Braun Dr. C. Batur _______________________________ _______________________________ Committee Member Dean of the College Dr. J. Drummond Dr. G. K. Haritos _______________________________ _______________________________ Committee Member Dean of the Graduate School Dr. S. I. Hariharan Dr. G. R. Newkome _______________________________ _______________________________ Committee Member Date R. C. Hendricks _______________________________ Committee Member Dr. A. Povitsky _______________________________ Committee Member Dr. G. Young ii ABSTRACT The relationship between the onset of Taylor instability and appearance of what is commonly known as “turbulence” in narrow gaps between two cylinders is investigated. A question open to debate is whether the flow formations observed during Taylor instability regimes are, or are related to the actual “turbulence” as it is presently modeled in micro-scale clearance flows. This question is approached by considering the viscous fluid flow in narrow gaps between two cylinders with various eccentricity ratios. The computational engine is provided by CFD-ACE+, a commercial multi-physics software. The flow patterns, velocity profiles and torques on the outer cylinder are determined when the speed of the inner cylinder, clearance and eccentricity ratio are changed on a parametric basis.
    [Show full text]
  • Experimental and Numerical Study of Taylor-Couette Flow" (2015)
    Iowa State University Capstones, Theses and Graduate Theses and Dissertations Dissertations 2015 Experimental and numerical study of Taylor- Couette flow Haoyu Wang Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/etd Part of the Mechanical Engineering Commons Recommended Citation Wang, Haoyu, "Experimental and numerical study of Taylor-Couette flow" (2015). Graduate Theses and Dissertations. 14462. https://lib.dr.iastate.edu/etd/14462 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Graduate Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. Experimental and numerical study of Taylor-Couette flow by Haoyu Wang A dissertation submitted to the graduate faculty in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Major: Mechanical Engineering Program of Study Committee: Michael G. Olsen, Major Professor Terry Meyer Shankar Subramaniam James Christian Hill Richard Dennis Vigil Iowa State University Ames, Iowa 2015 Copyright c Haoyu Wang, 2015. All rights reserved. ii TABLE OF CONTENTS LIST OF TABLES . iv LIST OF FIGURES . v ACKNOWLEDGEMENTS . xv ABSTRACT . xvi CHAPTER 1. INTRODUCTION . 1 General Introduction . .1 Dissertation Organization . .8 CHAPTER 2. POWER SPECTRUM ANALYSIS IN TAYLOR-COUETTE FLOW ......................................... 9 Abstract . .9 Introduction . 10 Experiment Apparatus and Procedure . 13 Data analysis . 17 Results and Discussion . 20 Summary and Conclusion . 28 CHAPTER 3. NUMERICAL INVESTIGATION OF TAYLOR-COUETTE FLOW WITH k − " MODEL . 43 Abstract . 43 Introduction .
    [Show full text]
  • Computational Study of Couette Flow Between Parallel Plates for Steady and Unsteady Cases Y
    EG0800331 Computational Study of Couette Flow Between Parallel Plates for Steady and Unsteady Cases Y. Rihan Atomic Energy Authority, Hot Lab. Centre, Egypt ABSTRACT Couette flow between parallel plates is a classical problem that has important applications in various industrial processing. In this investigation an analytical solution was obtained to predict the steady and unsteady Couette flow between parallel plates. One of the plates was stationary and the other plate moved with constant velocity. The governing partial differential equations were solved numerically using Crank-Nicolson implicit method to represent the flow behavior of the fluid. Key Words: Couette flow/ modeling/ parallel plates/ steady/ unsteady. INTRODUCTION Couette flow is a classical problem of primary importance in the history of fluid mechanics (1-4), which is a typical example of exact solutions for Navier-Stokes equation. Couette flow is perhaps the simplest of all viscous flows, while at the same time retaining much of the same physical characteristics of a more complicated boundary-layer flow. One of the most important process in industry is extrusion. Since the gap between the barrel and the screw of extruder is small, assuming a fluid flowing between parallel plates leads to representative results. There exist a large number of parameters in extrusion process which influence significantly the production rate and the quality of the final product. Couette flow between parallel plates is a classical problem that has important applications in power generators and pumps, etc. Several investigations have been done in this type of flow (5- 10). Etemad et al. (11) solved the simultaneously developed case of the motion and energy equation for power law fluid between parallel stationary plates when the variation of viscosity with temperature and viscous dissipation could not be neglected.
    [Show full text]
  • Electro-Osmotic Couette Flow with Joule Heating Effect
    The current issue and full text archive of this journal is available on Emerald Insight at: https://www.emerald.com/insight/2634-2499.htm Flow control in Flow control in microfluidics microfluidics devices: electro-osmotic Couette devices flow with joule heating effect C. Ahamed Saleel and Saad Ayed Alshahrani Mechanical Engineering Department, College of Engineering, King Khalid University, Abha, Saudi Arabia Received 30 March 2021 Revised 27 May 2021 Asif Afzal Accepted 9 June 2021 Mechanical Engineering, PA College of Engineering, Mangalore, India Maughal Ahmed Ali Baig Mechanical Engineering, CMR Technical Campus, Secunderabad, India, and Sarfaraz Kamangar and T.M. Yunus Khan Mechanical Engineering Department, College of Engineering, King Khalid University, Abha, Saudi Arabia Abstract Purpose – Joule heating effect is a pervasive phenomenon in electro-osmotic flow because of the applied electric field and fluid electrical resistivity across the microchannels. Its effect in electro-osmotic flow field is an important mechanism to control the flow inside the microchannels and it includes numerous applications. Design/methodology/approach – This research article details the numerical investigation on alterations in the profile of stream wise velocity of simple Couette-electroosmotic flow and pressure driven electro-osmotic Couette flow by the dynamic viscosity variations happened due to the Joule heating effect throughout the dielectric fluid usually observed in various microfluidic devices. Findings – The advantages of the Joule heating effect are not only to control the velocity in microchannels but also to act as an active method to enhance the mixing efficiency. The results of numerical investigations reveal that the thermal field due to Joule heating effect causes considerable variation of dynamic viscosity across the microchannel to initiate a shear flow when EDL (Electrical Double Layer) thickness is increased and is being varied across the channel.
    [Show full text]
  • Grain Flow As a Fluid-Mechanical Phenomenon
    J. Fluid lllech. (1983), 1•o/. 134, pp. 401-430 401 Printed in Great Britain Grain flow as a fluid-mechanical phenomenon ByP. K. HAFF Division of Physics, Mathematics and Astronomy, California Institute of Technology, Pasadena, California 91125 (Received 26 February 1982 and in revised form 7 April 1983) The behaviour of granular material in motion is studied from a continuum point of view. Insofar as possible, individual grains are treated as the 'molecules' of a granular 'fluid'. Besides the obvious contrast in shape, size and mass, a key difference between true molecules and grains is that collisions of the latter are inevitably inelastic. This, together with the fact that the fluctuation velocity may be comparable to the flow velocity, necessitates explicit incorporation of the energy equation, in addition to the continuity and momentum equations, into the theoretical description. Simple 'microscopic' kinetic models are invoked for deriving expressions for the 'coefficients' of viscosity, thermal diffusivity and energy absorption due to collisions. The 'coefficients' are not constants, but are functions of the local state of the medium, and therefore depend on the local 'temperature' and density. In general the resulting equations are nonlinear and coupled. However, in the limit 8 ~ d, where 8 is the mean separation between neighbouring grain surfaces and dis a grain diameter, the above equations become linear and can be solved analytically. An important dependent variable, in this formulation, in addition to the flow velocity u, is the mean random fluctuation ('thermal') velocity v of an individual grain. With a sufficient flux of energy supplied to the system through the boundaries of the container, v can remain non-zero even in the absence of flow.
    [Show full text]
  • Math 6880 : Fluid Dynamics I Chee Han Tan Last Modified
    Math 6880 : Fluid Dynamics I Chee Han Tan Last modified : August 8, 2018 2 Contents Preface 7 1 Tensor Algebra and Calculus9 1.1 Cartesian Tensors...................................9 1.1.1 Summation convention............................9 1.1.2 Kronecker delta and permutation symbols................. 10 1.2 Second-Order Tensor................................. 11 1.2.1 Tensor algebra................................ 12 1.2.2 Isotropic tensor................................ 13 1.2.3 Gradient, divergence, curl and Laplacian.................. 14 1.3 Generalised Divergence Theorem.......................... 15 2 Navier-Stokes Equations 17 2.1 Flow Maps and Kinematics............................. 17 2.1.1 Lagrangian and Eulerian descriptions.................... 18 2.1.2 Material derivative.............................. 19 2.1.3 Pathlines, streamlines and streaklines.................... 22 2.2 Conservation Equations............................... 26 2.2.1 Continuity equation.............................. 26 2.2.2 Reynolds transport theorem......................... 28 2.2.3 Conservation of linear momentum...................... 29 2.2.4 Conservation of angular momentum..................... 31 2.2.5 Conservation of energy............................ 33 2.3 Constitutive Laws................................... 35 2.3.1 Stress tensor in a static fluid......................... 36 2.3.2 Ideal fluid................................... 36 2.3.3 Local decomposition of fluid motion..................... 38 2.3.4 Stokes assumption for Newtonian fluid..................
    [Show full text]
  • Some Analytical Solutions of Laminar and Incompressible Flows of Viscid Fluids
    DSpace Institution DSpace Repository http://dspace.org Mathematics Thesis and Dissertations 2017-10-11 Some Analytical Solutions of Laminar and Incompressible Flows of Viscid Fluids Tadesse, Zenebe http://hdl.handle.net/123456789/7899 Downloaded from DSpace Repository, DSpace Institution's institutional repository Some Analytical Solutions of Laminar and Incompressible Flows of Viscid Fluids By Tadesse Zenebe Mesfin Department of Mathematics Collage of Science Bahir Dar University September, 2017 Bahirdar, Ethiopia 1 Some Analytical Solutions of Laminar and Incompressible Flows of Viscous Fluids A Dissertation Submitted in Partial Fulfillment of the Requirements for the Degree of Master of Science in Mathematics. By Tadesse Zenebe Mesfin Adivisor: Dr. Eshetu Haile Department of Mathematics Collage of Science Bahir Dar University September, 2017 Bahirdar, Ethiopia 2 The Dissertation Entitled “Some Analytical Solutions of Laminar and Incompressible Flows of Viscous Fluids” by Tadesse Zenebe is approved for the Degree of Master of Science in Mathematics. Board of Examiners Name Signature Adviser: Dr. Eshetu Haile ----------------- Examiner 1:-------------------- --------------- Examiner 2:-------------------- ------------------ Date--------------- 3 Acknowledgements First, I would like to thank Dr. Eshetu Haile for his continuous support by giving source of reading material, unreserved advice and guidance by reading my project and giving constructive comments which helped me to arrange the report. I am grateful to Tewodros higher preparatory and secondary school teachers who gave me helpful advice and comments. Finally, I want to thank information technology professional of our school for helping computer related work. i Abstract This project work is concerned about some simple analytical solutions of laminar and incompressible viscous fluid flows. Particularly it deals about the velocity distributions of some simple fluid flow problems (Couette and Poisueille) flows.
    [Show full text]
  • Pallavi Bhambri
    Drag reduction using additives in a Taylor-Couette Flow by Pallavi Bhambri A thesis submitted in partial fulfillment of the requirements for the degree of Master of Science Department of Mechanical Engineering University of Alberta © Pallavi Bhambri, 2016 ABSTRACT The current study investigates the drag reduction (DR) using high molecular weight polymers such as commercial polyacrylamide, polysaccharides and thermo-responsive polymers. A Taylor-Couette (TC) setup was designed and fabricated to examine the abovementioned polymers for drag reduction, and to demonstrate that turbulent Taylor-Couette testing is a convenient and cost effective analogue for pipe flow drag reduction. Initial experiments were conducted with water as a working fluid and the dimensionless torque was used to scale the torque which compared well with the previous TC studies. Further, the results obtained were found to scale well with the turbulent drag in wall bounded shear flows (such as pipe/channel flow). Using TC flow, commercial polyacrylamide along with polysaccharides such as aloe vera, pineapple fibers, tamarind powder and cellulose nano crystals (CNC) were studied for DR. The effect of Reynolds number (Re) and concentration of these high molecular weight polymers was observed. Polysaccharides are environmentally friendly and offer a huge advantage over commercial polymers due to their biodegradable nature. Furthermore, the high molecular weight polymers are also used extensively in oil recovery during hydraulic fracturing for DR. However, due to their long chain length, these polymers get adsorbed on the surface of reservoir, diminishing the effectiveness of fracking. Hence, this study was then extended to Poly-(N-isopropylacrylamide) (PNIPAM), a thermoresponsive polymer.
    [Show full text]
  • Processing the Couette Viscometry Data Using a Bingham Approximation in Shear Rate Calculation Patrice Estellé, Christophe Lanos, Arnaud Perrot
    Processing the Couette viscometry data using a Bingham approximation in shear rate calculation Patrice Estellé, Christophe Lanos, Arnaud Perrot To cite this version: Patrice Estellé, Christophe Lanos, Arnaud Perrot. Processing the Couette viscometry data using a Bingham approximation in shear rate calculation. Journal of Non-Newtonian Fluid Mechanics, Elsevier, 2008, 154, pp.31-38. 10.1016/j.jnnfm.2008.01.006. hal-00664433 HAL Id: hal-00664433 https://hal.archives-ouvertes.fr/hal-00664433 Submitted on 30 Jan 2012 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Processing the Couette viscometry data using a Bingham approximation in shear rate calculation Patrice Estellé 1, *, Christophe Lanos 1, Arnaud Perrot 2 1 LGCGM, Département Matériaux et Thermo-Rhéologie, Institut Universitaire Technologique, rue du Clos Courtel, BP 90422, 35704 Rennes Cedex 7, France 2 LG2M, Université de Bretagne Sud, Rue Saint Maudé, 56321 Lorient Cedex, France ∗ Author to whom correspondence should be addressed. Electronic mail: [email protected] Tel: +33 (0) 23 23 42 00 Fax: +33 (0) 2 23 23 40 51 Abstract: This paper presents an approach to computing the shear flow curve from torque-rotational velocity data in a Couette rheometer.
    [Show full text]
  • On the Plane Couette Flow of a Viscous Compressible Fluid with Transpiration Cooling
    ON THE PLANE COUETTE FLOW OF A VISCOUS COMPRESSIBLE FLUID WITH TRANSPIRATION COOLING J. L. BAI~AL AND N. C. JAIN [Oepartment of Mathematics, University of Jodhpur, Jodhpur {India)] Received Dr 13, 1973 (Communicated by Prof. J. N. Kapur, v..~.sc.) Ansr~cr The exact solution for the plane couette flow of a viseous compres- sible, heat conducting, perfect gas with the same gas injection at the stationary plate and its corresponding removal at the moving plate has been studied. It is found that the gas injection is very helpful in reducing the temperature recovery factor. Effects of injection on the shearing stress at the lower plate, longitudinal velocity pro¡ and the enthalpy arr shown graphically. 1. NOMENCLATURE E Eckert number, = (~ -- 1 ) M| ~ TI . T1 -- To b distance between the plates; h* defined by equation (30); H enthalpy, = cpT ; H* = H/Ha ; Ha* dimensionless adiabatie wall enthalpy; M,, Maeh number ; P pressure; p* dimensionless pressure, = p/plU ~; Pr Prandfl number ; Ha* -- 1 rŸ recovery factor, = (7- 1)M,, ~ ; A l~July, 74 2 J. L. BANSAL AND N. C. JAtN Re Renolds number, = piUb//zx ; T tcmpcrature; U vclocity componcnt along the x axis; U* dimensionless axial velocity, = u/U; U vclocity of the moving platc; q) vclocity componcnt perpendicular to the x-axis dimensionless trartsverse velocity, = v/U ; X axial distance from the entrance of the chanrtel; Y perpendicular distance from the x-axis; Greek Symbols : 7 isentropic exponent, = c~/cv ; dimensionless transverse distance, = y/b ; injection parameter, ---- povob/tz~ ; tz viscosity; t. dimensiouless viscosity, = /~/tzl ; P density ; p* dimensionless density, = p/pl ; T o dimensionless shearing stress de¡ by equation (16); Subscripts : 0, 1 values of the variables at the stationary and moving plate respectively.
    [Show full text]