Academic literature on the topic 'Non-Newtonian fluid mechanics'

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Journal articles on the topic "Non-Newtonian fluid mechanics"

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de Souza Mendes, Paulo R. "Dimensionless non-Newtonian fluid mechanics." Journal of Non-Newtonian Fluid Mechanics 147, no. 1-2 (November 2007): 109–16. http://dx.doi.org/10.1016/j.jnnfm.2007.07.010.

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Knight, D. G. "Revisiting Newtonian and non-Newtonian fluid mechanics using computer algebra." International Journal of Mathematical Education in Science and Technology 37, no. 5 (July 15, 2006): 573–92. http://dx.doi.org/10.1080/03091900600712215.

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MAYNE, GEORGES. "GEOMETRICAL METHOD IN NON-NEWTONIAN FLUID MECHANICS." Quarterly Journal of Mechanics and Applied Mathematics 42, no. 2 (1989): 239–47. http://dx.doi.org/10.1093/qjmam/42.2.239.

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ALBAALBAKI, BASHAR, and ROGER E. KHAYAT. "Pattern selection in the thermal convection of non-Newtonian fluids." Journal of Fluid Mechanics 668 (January 5, 2011): 500–550. http://dx.doi.org/10.1017/s0022112010004775.

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The thermogravitational instability in a fluid layer of a non-Newtonian medium heated from below is investigated. Linear and weakly nonlinear analyses are successively presented. The fluid is assumed to obey the Carreau–Bird model. Although the critical threshold is the same as for a Newtonian fluid, it is found that non-Newtonian fluids can convect in the form of rolls, squares or hexagons, depending on the shear-thinning level. Similar to Newtonian fluids, shear-thickening fluids convect only in the form of rolls. The stability of the convective steady branches is carried out to determine under which specific conditions a pattern is preferred. The influence of the rheological and physical parameters is examined and discussed in detail.
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Bullough, W. A., G. E. Cardew, J. Kinsella, and F. E. Boysan. "CFM Self-Teaching in the Fluids Laboratory: Newtonian and Non-Newtonian Flow in Circular Pipes." International Journal of Mechanical Engineering Education 26, no. 3 (July 1998): 167–76. http://dx.doi.org/10.1177/030641909802600301.

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Experiences of a computer fluid mechanics based self-teaching exercise on the flow of Newtonian and non-Newtonian fluids are reported. This was restricted to the steady flow of fluids in circular pipes. The work involved keyboard-literate students in the first year of a mechanical engineering degree course finding the pipe design laws, in terms of the effects of diameter and pressure gradient increase on flow rate. Also, velocity profile plus development length effects, not easily taught via analytical or laboratory classes, were illustrated.
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Spodareva, L. A. "Stability of non-newtonian fluid flows." Journal of Applied Mechanics and Technical Physics 41, no. 3 (May 2000): 446–51. http://dx.doi.org/10.1007/bf02465294.

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Akbarzadeh, Pooria, Mahmood Norouzi, Reza Ghasemi, and Seyed Zia Daghighi. "Experimental study on the entry of solid spheres into Newtonian and non-Newtonian fluids." Physics of Fluids 34, no. 3 (March 2022): 033111. http://dx.doi.org/10.1063/5.0081002.

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This study experimentally investigates the entry of hydrophobic/hydrophilic spheres into Newtonian and Boger fluids. By considering solution of 82% glycerin and 18% water and solution of 80% glycerin, 20% water and 100 ppm polyacrylamide, Newtonian and Boger fluids are made, respectively. It has been tried that liquids' surface tension, density, and viscosity are almost the same. Thus, all dimensionless numbers are approximately the same at a similar impact velocity except for the elasticity number. A PcoDimaxS highspeed camera captures the spheres' trajectory from the impact to the end of the path. Regarding the range of released height ([Formula: see text]), the impact velocities are approximately in the range of [Formula: see text]. The role of fluid elasticity in combination with the sphere surface wettability on the air cavity formation/evolution/collapse is mainly studied. Also, the kinetics of the sphere motion (velocity, acceleration, and hydrodynamic force coefficient) is studied. The results show that air drawn due to the sphere's impact with the Newtonian liquid is more, and the pinch-off takes place later. Also, shedding bubbles are cusped-shaped in the Boger fluid, while in the Newtonian fluid, they are elliptical. In addition, the most significant impact of surface wettability is observed in the Newtonian fluid. Finally, the results reveal that the sphere in the Newtonian fluid can move faster and travel a longer distance in a specific time interval. The differences observed are closely related to the viscoelastic fluid's elasticity property and extensional viscosity.
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Shan, Jie, and Xiaojun Zhou. "The Effect of Bubbles on Particle Migration in Non-Newtonian Fluids." Separations 8, no. 4 (March 24, 2021): 36. http://dx.doi.org/10.3390/separations8040036.

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The movement of the gas–liquid interface caused by the movement of the bubble position will have an impact on the starting conditions for particle migration. This article quantifies the influence of moving bubbles on the starting conditions of particle migration in non-Newtonian fluids, and it aims to better understand the influence of bubbles moving in non-Newtonian fluids on particle migration to achieve more effective control. First, the forces and moments acting on the particles are analyzed; then, fluid dynamics, non-Newtonian fluid mechanics, extended DLVO (Derjaguin Landau Verwey Overbeek theory), surface tension, and friction are applied on the combined effects of particle migration. Then, we reasonably predict the influence of gas–liquid interface movement on particle migration in non-Newtonian fluids. The theoretical results show that the movement of the gas–liquid interface in non-Newtonian fluids will increase the separation force acting on the particles, which will lead to particle migration. Second, we carry out the particle migration experiment of moving bubbles in non-Newtonian fluid. Experiments show that when the solid–liquid two-phase flow is originally stable, particle migration occurs after the bubble movement is added. This phenomenon shows that the non-Newtonian fluid with bubble motion has stronger particle migration ability. Although there are some errors, the experimental results basically support the theoretical data.
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Sirivat, A., K. R. Rajagopal, and A. Z. Szeri. "An experimental investigation of the flow of non-Newtonian fluids between rotating disks." Journal of Fluid Mechanics 186 (January 1988): 243–56. http://dx.doi.org/10.1017/s0022112088000126.

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The results of an experimental investigation on the flow of a non-Newtonian fluid between rotating, parallel disks are described in this paper. These results are qualitatively different from those exhibited by linearly viscous fluids in that a narrow layer of exceedingly high velocity gradients appears in the non-Newtonian fluid.
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Dai, F., and M. M. Khonsari. "A Theory of Hydrodynamic Lubrication Involving the Mixture of Two Fluids." Journal of Applied Mechanics 61, no. 3 (September 1, 1994): 634–41. http://dx.doi.org/10.1115/1.2901507.

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Based on the principles of continuum mechanics, we drive the governing equations for the hydrodynamic lubrication involving the mixture of two incompressible fluids. The governing equations are general in the sense that they can be applied to the mixture of any simple non-Newtonian fluid with a Newtonian fluid. A mixture thus formed is considered to be nonhomogeneous and non-Newtonian. In the theoretical development, the interaction between the constituents is taken into consideration. It is shown that a number of currently available models are special cases of the theory presented in this paper. As an example, results are presented for journal bearing performance lubricated with a mixture of a power-law fluid mixed with Newtonian oil.
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Dissertations / Theses on the topic "Non-Newtonian fluid mechanics"

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Keiller, Robert A. "Non-Newtonian extensional flows." Thesis, University of Cambridge, 1991. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.315030.

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Gouldson, Iain William. "The flow of Newtonian and non-Newtonian fluids in an annular geometry." Thesis, University of Liverpool, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.243035.

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Mennad, Abed. "Singular behaviour of Non-Newtonian fluids." Thesis, Peninsula Technikon, 1999. http://hdl.handle.net/20.500.11838/1253.

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Thesis (MTech (Mechanical Engineering))--Peninsula Technikon, 1999
Since 1996, a team at the Centre for Research in Applied Technology (CRATECH) at Peninsula Technikon, under NRF sponsorship and with industrial co-operation, has been involved in the simulation of Non-Newtonian flow behaviour in industrial processes, in particular, injection moulding of polymers. This study is an attempt to deal with some current issues of Non-Newtonian flow, in small areas, from the viewpoint of computational mechanics. It is concerned with the numerical simulation of Non-Newtonian fluid flows in mould cavities with re-entrant corners. The major complication that exists in this numerical simulation is the singularity of the stresses at the entry of the corner, which is responsible for nonintegrable stresses and the propagation of solution errors. First, the study focuses on the derivation of the equations of motion of the flow which leads to Navier- Stokes equations. Thereafter, the occurrence of singularities in the numerical solution of these equations is investigated. Singularities require special attention no matter what numerical method is used. In finite element analysis, local refinement around the singular point is often employed in order to improve the accuracy. However, the accuracy and the rate of convergence are not, in general, satisfactory. Incorporating the nature of singularity, obtained by an asymptotic analysis in the numerical solution, has proven to be a very effective way to improve the accuracy in the neighborhood of the singularity and, to speed up the rate of convergence. This idea has been successfully adopted in solving mainly fracture mechanics problems by a variety of methods: finite difference, finite elements, boundary and global elements, and spectral methods. In this thesis, the singular finite elements method (SFEM), similar in principle to the crack tip element used in fracture mechanics, is proposed to improve the solution accuracy in the vicinity of the singular point and to speed up the rate of convergence. This method requires minor modifications to standard finite element schemes. Unfortunately, this method could not be implemented in this study due to the difficulty in generating the mesh for the singular element. Only the standard finite element method with mesh refinement has been used. The results obtained are in accordance with what was expected.
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Van, Sittert Fritz Peter. "The effect of pipe roughness on non-Newtonian turbulent flow." Thesis, Cape Technikon, 1999. http://hdl.handle.net/20.500.11838/1035.

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Thesis (MTech (Civil Engineering))--Cape Technikon, Cape Town, 1999
Pipe roughness is known to greatly increase the turbulent flow friction factor for Newtonian fluids. The well-known Moody diagram shows that an order of magnitude increase in the friction is possible due to the effect of pipe roughness. However, since the classical work of Nikuradse (1926 -1933), very little has been done in this area. In particular, the effects that pipe roughness might have on non-Newtonian turbulent flow head loss, has been all but totally ignored. This thesis is directed at helping to alleviate this problem. An experimental investigation has been implemented in order to quantify the effect that pipe roughness has on non-Newtonian turbulent flow head loss predictions. The Balanced Beam Tube Viscometer (BBTV), developed at the University of Cape Town, has been rebuilt and refined at the Cape Technikon and is being used for research in this field. The BBTV has been fitted with pipes of varying roughness. The roughness of smooth P\'C pipes was artificially altered using methods similar to those of Nikuradse. This has enabled the accumulation of flow data in laminar and turbulent flow in pipes that are both hydraulically smooth and rough Newtonian and non-Newtonian fluids have been used for the tests. The data have been subjected to analysis using various theories and scaling laws. The strengths and problems associated with each approach are discussed and It is concluded that roughness does have a significant effect on Newtonian as well as non-Newtonlan flow.
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Lockett, Timothy James. "Numerical simulation of inelastic non-Newtonian fluid flows in annuli." Thesis, Imperial College London, 1992. http://hdl.handle.net/10044/1/8422.

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Yim, Samson Sau Shun. "The effect of flow stability on residence time distribution of Newtonian and non-Newtonian liquids in couette flow." Thesis, University College London (University of London), 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.264191.

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Goshawk, Jeffrey Alan. "Enhancement of the drainage of non-Newtonian liquid films by oscillation." Thesis, University of Liverpool, 1992. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.333685.

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Kabamba, Batthe Matanda. "Evaluation of centrifugal pump performance derating procedures for non-Newtonian slurries." Thesis, Cape Peninsula University of Technology, 2006. http://hdl.handle.net/20.500.11838/2170.

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Thesis (MTech(Civil Engineering))--Cape Peninsula University of Technology, 2006.
The performance of a centrifugal pump is altered for slurry or viscous materials (Stepanoff, 1969) and this needs to be accounted for. Usually, the suitable selection and evaluation of centrifugal pumps is based only on water pump performance curves supplied by the pump manufacturer (Wilson, Addie, Sellgren & Clift, 1997). In 1984 Walker and Goulas conducted a number of pump performance tests with kaolin clay slurries and coal slurries on a Warman 4/3 AH horizontal slurry pump and a Hazleton 3-inch B CTL horizontal pump (Walker and Goulas, 1984). Walker and Goulas have analysed the test data and correlated the performance derating both at the best efficiency flow rate (BEP) and at 10% of the best efficiency flow rate (0.1 BEP) to the modified pump Reynolds number (NRep). They have noticed that the head and the efficiency reduction ratio decreased for the pump Reynolds number less then 10⁶. Furthermore, Walker and Goulas obtained a reasonably good agreement (± 5%) between pump test data for non-Newtonian materials and pump performance prediction using the Hydraulics Institute chart. Sery and Slatter (2002) have investigated pump deration for non-Newtonian yield pseudoplastic materials. The NRep was calculated using the Bingham plastic viscosity (µp). Results have shown good agreement with regard to head and efficiency reduction ratios in comparison with previous work. However, Sery and Slatter's pump performance correlation using the HI chart did not reach the same conclusion. Error margin of ± 20% and ± 10% were found for head and efficiency respectively. This study is an attempt to reconcile the differences between Walker and Goulas (1984) and Sery and Slatter (2002) and extend the evaluation of these derating methods to pseudoplastic materials. The test work was conducted in the Flow Process Research Centre laboratory of the Cape Peninsula University of Technology using two centrifugal pumps; a Warman 6/4 and a GrW 4/3. The materials used were water, CMC solution bentonite and kaolin suspension at different concentrations (7% and 9% by weight for bentonite; 5%, 6% and 7% by weight for CMC; 17%, 19% and 21% by volume for kaolin).
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Kheng, Tan Ka. "Gas diffusion into viscous and non-Newtonian liquids and the onset of convection." Thesis, University of Cambridge, 1994. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.321528.

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Thorvaldsen, Gary Sven. "The effect of the particle size distribution on non-Newtonian turbulent slurry flow in pipes." Thesis, Cape Technikon, 1996. http://hdl.handle.net/20.500.11838/896.

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Thesis (MTech (Chemical Engineering))--Cape Technikon, Cape Town,1996
The handling of solid-liquid suspensions is an important concern within the chemical and processing industries and many theoretical models have been proposed to try and explain and predict turbulent flow behaviour. However, the prediction of turbulent flow from only the viscous properties of non-Newtonian suspensions has over the years been questioned by researchers. This thesis considers theoretical models well established in the literature and the Slatter model, which uses both the rheology of the suspension and the particle size distribution of the solids. These models are used to analyze the experimental data and the effect that particle size and the particle size distribution has on turbulent flow behaviour. The literature concerning the rheological fundamentals relevant to fluid flow in pipes has been examined. The Newtonian turbulent flow model as well as the non-Newtonian models of Dodge & Metzner, Torrance, Kemblowski & Kolodziejski, Wilson & Thomas and Slatter have been reviewed. Test work was conducted at the University of Cape Town's Hydrotransport Research Laboratory using a pumped recirculating pipe test rig. The test apparatus has been fully described and calibration and test procedures to enable collecting of accurate pipeline data have been presented. Three slurries were used in test work namely kaolin clay, mixture I (kaolin clay and rock flour) and mixture 2 (kaolin clay, rock flour and sand) with ad,s particle size ranging from 24/Lm to 170/Lm. The yield pseudoplastic model has been used to model and predict the laminar flow of the suspensions that were tested and the meth9J adopted by Neill (1988) has been used to determine the rheological constants. The pipeline test results have been presented as pseudoshear diagrams together with the theoretical model lines providing a visual appraisal of the performance of each model. The Slatter model predicts the test data best with the other theoretical models that were considered tending to under predict the head loss. The reason the Slatter model performs better than the other theoretical models is because this model can account for the wall roughness and particle roughness effect. Evidence to support this statement has been presented. This thesis highlights the fact that the particle size distribution is a vitally important property of the suspension and that it does influence turbulent flow behaviour. It shows that turbulence modelling using the particle roughness effect (eg Slatter, 1994) is valid and can be adopted for non-Newtonian slurries. It is concluded that the particle size distribution must be used to determine the particle roughness effect and this effect must be incorporated in the turbulent flow analysis of non-Newtonian slurries.
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Books on the topic "Non-Newtonian fluid mechanics"

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Böhme, G. Non-Newtonian fluid mechanics. Amsterdam: North-Holland, 1987.

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Farina, Angiolo, Lorenzo Fusi, Andro Mikelić, Giuseppe Saccomandi, Adélia Sequeira, and Eleuterio F. Toro. Non-Newtonian Fluid Mechanics and Complex Flows. Edited by Angiolo Farina, Andro Mikelić, and Fabio Rosso. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-74796-5.

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I͡Ankov, Viktor Ivanovich. Osnovy mekhaniki nenʹi͡utonovskikh zhidkosteĭ: Uchebnoe posobie. Tverʹ: Tverskoĭ politekhn. in-t, 1991.

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Bubbles, drops, and particles in non-Newtonian fluids. 2nd ed. Boca Raton, FL: CRC Taylor & Francis, 2007.

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Richardson, J. F. (John Francis), Knovel (Firm), and ScienceDirect (Online service), eds. Non-Newtonian flow and applied rheology: Engineering applications. 2nd ed. Amsterdam: Butterworth-Heinemann/Elsevier, 2008.

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Bubbles, drops, and particles in non-Newtonian fluids. Boca Raton, Fla: CRC Press, 1993.

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International, Workshop on Numerical Methods for Non-Newtonian Flows (12th 2001 Monterey Bay Calif ). XIIth International Workshop on Numerical Methods for Non-Newtonian Flows. Amsterdam: Elsevier, 2002.

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Meeting, American Society of Mechanical Engineers Winter. Recent advances in non-newtonian flows: Presented at the Winter Annual Meeting of the American Society of Mechanical Engineers, Anaheim, California, November 8-13, 1992. New York, N.Y: American Society of Mechanical Engineers, 1992.

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Zhou cheng jian xi fei niu dun run hua ji de fei xian xing dong li xue. Beijing Shi: Beijing li gong da xue chu ban she, 2009.

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service), SpringerLink (Online, ed. Cavitation in Non-Newtonian Fluids: With Biomedical and Bioengineering Applications. Berlin, Heidelberg: Springer-Verlag Berlin Heidelberg, 2011.

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Book chapters on the topic "Non-Newtonian fluid mechanics"

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Nijenhuis, Klaas, Gareth McKinley, Stephen Spiegelberg, Howard Barnes, Nuri Aksel, Lutz Heymann, and Jeffrey Odell. "Non-Newtonian Flows." In Springer Handbook of Experimental Fluid Mechanics, 619–743. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-30299-5_9.

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Irgens, Fridtjov. "Basic Equations in Fluid Mechanics." In Rheology and Non-Newtonian Fluids, 25–61. Cham: Springer International Publishing, 2013. http://dx.doi.org/10.1007/978-3-319-01053-3_3.

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Bush, M. B. "Applications in Non-Newtonian Fluid Mechanics." In Viscous Flow Applications, 134–60. Berlin, Heidelberg: Springer Berlin Heidelberg, 1989. http://dx.doi.org/10.1007/978-3-642-83683-1_7.

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Lyubimova, T. P. "Thermal Convection of Non-Newtonian Fluids under Low Gravity Conditions." In Microgravity Fluid Mechanics, 555–62. Berlin, Heidelberg: Springer Berlin Heidelberg, 1992. http://dx.doi.org/10.1007/978-3-642-50091-6_57.

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Jones, R. N., and K. Walters. "The Basic Equations of Non-Newtonian Fluid Mechanics." In Rheological Fundamentals of Polymer Processing, 1–36. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-015-8571-2_1.

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Draad, Aswin A., and Martien A. Hulsen. "Transition From Laminar to Turbulent Flow for Non-Newtonian Fluids." In Fluid Mechanics and Its Applications, 105–10. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0457-9_21.

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Malkus, David S., John A. Nohel, and Bradley J. Plohr. "Oscillations in Piston-Driven Shear Flow of a Non-Newtonian Fluid." In Fluid Mechanics and Its Applications, 57–71. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0191-2_5.

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Janela, João, Alexandra Moura, and Adélia Sequeira. "Towards a Geometrical Multiscale Approach to Non-Newtonian Blood Flow Simulations." In Advances in Mathematical Fluid Mechanics, 295–309. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-04068-9_18.

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Farina, Angiolo, Lorenzo Fusi, Andro Mikelić, Giuseppe Saccomandi, Adélia Sequeira, and Eleuterio F. Toro. "Correction to: Non-Newtonian Fluid Mechanics and Complex Flows." In Lecture Notes in Mathematics, E1. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-74796-5_6.

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Steffe, James F., and Robert Y. Ofoli. "Food Engineering Problems in Rheology and Non-Newtonian Fluid Mechanics." In Food Properties and Computer-Aided Engineering of Food Processing Systems, 313–16. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-2370-6_21.

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Conference papers on the topic "Non-Newtonian fluid mechanics"

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Baumert, H. Z., and B. Wessling. "TURBULENT MIXING IN NON-NEWTONIAN DISPERSIONS." In Topical Problems of Fluid Mechanics 2016. Institute of Thermomechanics, AS CR, v.v.i., 2016. http://dx.doi.org/10.14311/tpfm.2016.002.

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Bertola, Volfango, and Emilio Cafaro. "Formal Analogy Between Non-Newtonian Flows and Compressible Flows." In 3rd Theoretical Fluid Mechanics Meeting. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2002. http://dx.doi.org/10.2514/6.2002-3078.

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"Dissipative properties of non-Newtonian fluid under impact load." In Engineering Mechanics 2018. Institute of Theoretical and Applied Mechanics of the Czech Academy of Sciences, 2018. http://dx.doi.org/10.21495/91-8-321.

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Di Federico, V., S. Cintoli, and G. Bizzarri. "Viscous spreading of non-Newtonian gravity currents in radial geometry." In ADVANCES IN FLUID MECHANICS 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/afm06040.

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Šedivý, Dominik, Simona Fialová, and Darina Jašíková. "Flow of Newtonian and non-Newtonian fluid through pipe with flexible wall." In 37TH MEETING OF DEPARTMENTS OF FLUID MECHANICS AND THERMODYNAMICS. Author(s), 2018. http://dx.doi.org/10.1063/1.5049922.

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Caggio, M., and Š. Nečasová. "NOTE ON THE PROBLEM OF COMPRESSIBLE NON-NEWTONIAN FLUIDS." In Topical Problems of Fluid Mechanics 2019. Institute of Thermomechanics, AS CR, v.v.i., 2019. http://dx.doi.org/10.14311/tpfm.2019.005.

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Ugarelli, R., M. Bottarelli, and V. Di Federico. "Displacement of non-Newtonian compressible fluids in plane porous media flow." In ADVANCES IN FLUID MECHANICS 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/afm080231.

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Dominik, Šedivý, Ferfecki Petr, and Fialová Simona. "Force effects on rotor of squeeze film damper using Newtonian and non-Newtonian fluid." In 36TH MEETING OF DEPARTMENTS OF FLUID MECHANICS AND THERMODYNAMICS. Author(s), 2017. http://dx.doi.org/10.1063/1.5004368.

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Ma, Jingtao \Wang, Li and Fang-Bao Tian. "IB-LBM study of non-Newtonian flexible capsule flows in contraction-expansion microchannels." In 22nd Australasian Fluid Mechanics Conference AFMC2020. Brisbane, Australia: The University of Queensland, 2020. http://dx.doi.org/10.14264/6e15e3d.

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Vradis, George C. "Heat Transfer and Fluid Mechanics of Herschel-Bulkley Fluids." In ASME 1998 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 1998. http://dx.doi.org/10.1115/imece1998-0452.

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Abstract A comprehensive review of the heat transfer phenomena related to the flow of purely viscous non-Newtonian fluids exhibiting a yield stress in some simple and complex geometries is presented. Both attached and separated flows of Bingham and Herschel-Bulkley fluids are discussed. The presence of a yield-stress is shown to significantly impact the heat transfer and flow characteristics, as compared to those in the case of a Newtonian fluid, in particular in the cases where separation of the flow would be expected.
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