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Dissertations / Theses on the topic 'Non-Newtonian'

Author: Grafiati

Published: 4 June 2021

Last updated: 25 July 2025

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1

Lombe, Mubanga. "Spin coating of Newtonian and non-Newtonian fluids." Doctoral thesis, University of Cape Town, 2006. http://hdl.handle.net/11427/4904.

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2

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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3

Hockey, Randal Myles. "Turbulent Newtonian and non-Newtonian flows in a stirred reactor." Thesis, Imperial College London, 1990. http://hdl.handle.net/10044/1/46341.

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4

Ozgen, Serkan. "Two-layer flow stability in newtonian and non-newtonian fluids." Doctoral thesis, Universite Libre de Bruxelles, 1999. http://hdl.handle.net/2013/ULB-DIPOT:oai:dipot.ulb.ac.be:2013/211876.

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5

Chilcott, Mark David. "Mechanics of non-Newtonian fluids." Thesis, University of Cambridge, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.329946.

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6

Mansour, Mohamed Hassan. "Non-Newtonian flow in microvessels." Thesis, University of Southampton, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.523205.

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7

Fyrippi, Irene. "Flowmetering of non-Newtonian liquids." Thesis, University of Liverpool, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.400185.

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8

Whitelaw, David Stuart. "Droplet atomisation of Newtonian and non-Newtonian fluids including automotive fuels." Thesis, Imperial College London, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.266620.

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9

Poole, Robert John. "Turbulent flow of Newtonian and non-Newtonian liquids through sudden expansions." Thesis, University of Liverpool, 2002. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.399176.

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10

KONGARA, VEERA VENKATA SATYA SRINIVASU. "NONLINEAR STABILITY ANALYSIS OF VISCOUS NEWTONIAN AND NON-NEWTONIAN VISCOELASTIC SHEETS." University of Cincinnati / OhioLINK, 2006. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1163617690.

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11

Ducharme, Réjean 1970. "Capillary flow of non-Newtonian fluids." Thesis, McGill University, 1995. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=23392.

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The flow of a two-dimensional incompressible non-Newtonian fluid, showing a viscoelastic behavior, has been studied using the White-Metzner model with a phenomenological law for the viscosity, the Spriggs' truncated power-law model. Our goal was to determine if these models could generate the oscillating instabilities appearing in such fluids at very high driving force. We studied the effect of various quantities on the time-dependent numerical simulations and noticed that the mesh length was not very important for the accuracy of the results. However, the time constant modulus appearing in th

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12

Ross, Andrew Baxter. "Studies in non Newtonian coating flows." Thesis, University of Strathclyde, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.248600.

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13

ABDU, ALINE AMARAL QUINTELLA. "NON-NEWTONIAN FLUID DISPLACEMENT IN ANNULI." PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO, 2016. http://www.maxwell.vrac.puc-rio.br/Busca_etds.php?strSecao=resultado&nrSeq=29332@1.

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PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO<br>CONSELHO NACIONAL DE DESENVOLVIMENTO CIENTÍFICO E TECNOLÓGICO<br>Na indústria do petróleo são comuns processos envolvendo deslocamentos de um fluido pelo outro, como nos processos de completação e cimentação de poços. A eficiência desses deslocamentos é de suma importância, garantindo a vida útil do poço. A operação é considerada adequada quando ocorre uma distribuição homogênea da pasta de cimento na parede do poço. No presente trabalho um estudo experimental e numérico do deslocamento de fluidos em espaço anular foi realizada. Para os tes

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14

Chaffin, Stephen. "Non-Newtonian fluids in complex geometries." Thesis, University of Sheffield, 2017. http://etheses.whiterose.ac.uk/16750/.

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15

Alrashidi, Azizah. "Nonlinear control for non-Newtonian flows." Thesis, University of Birmingham, 2015. http://etheses.bham.ac.uk//id/eprint/5777/.

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PDE-constrained optimization is an important area in the field of numerical analysis, with problems arising in a wide variety of applications including optimal design, optimal control and parameter estimation. The aim of such problems is to minimize a functional J(u,d) whilst adhering to constraints posed by a system of partial differential equations (PDE), with u and d used respectively to denote the state and control of the system. In this thesis, we describe the steady-state generalized Stokes equations for incompressible fluids. We proceed to derive the weak formulation of the problem, and

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16

Kazadi, Dieudonne Matang'a. "Non-Newtonian losses through diaphragm valves." Thesis, Cape Peninsula University of Technology, 2005. http://hdl.handle.net/20.500.11838/904.

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Thesis (MTech (Chemical Engineering))--Cape Peninsula University of Technology, 2005<br>The prediction of head losses in a pipe system is very important because head losses affect the performance of fluid machinery such as pumps. In a pipe system, two kinds of losses are observed: major losses and minor losses. In Newtonian and non-Newtonian flow, major losses are those that are due to friction in straight pipes and minor losses are those that are due to pipe fittings such as contractions, expansions, bends and valves. Minor losses must be accurately predicted in a pipe system becaus

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17

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<br>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 moul

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18

Trinh, Khanh Tuoc. "Turbulent transport near the wall in newtonian and non-newtonian pipe flow." Thesis, University of Canterbury. Chemical Engineering, 1992. http://hdl.handle.net/10092/7693.

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Turbulence is present everywhere in our environment yet its complexities remain one of the great challenges in scientific and engineering research. This work began out of personal interest. As such, it involved all aspects of my background, not just my engineering training. It is disconcerting to some westerners to think of scientists as philosophers. In the traditional Vietnamese culture, it is not possible to think of scientists as not being philosophers. In the old days we taught philosophy before we gave more practical training because all that we do IS influenced by our beliefs. I was e

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19

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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20

Jaber, Othman Jamal Othman. "Flow-Blurring and Air-Assisted Atomization of Newtonian and Non-Newtonian Liquids." Thesis, The University of Sydney, 2022. https://hdl.handle.net/2123/28167.

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A comprehensive study on Flow-Focusing/Flow-Blurring (FF/FB) atomizers is presented in this study. A transparent FF/FB atomizer is introduced in this work to aid in the characterization of sprays emitting from both of the atomizer’s regimes. Newtonian and non-Newtonian liquids were tested over a wide range of operating conditions and laser diagnostics were employed to unveil the resulting structures and salient features of the sprays. Direct imaging of the atomizer’s liquid tube tip region enabled identification of the onset of the atomizer’s regime transition at different liquid tube recesse

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21

Amani, Ahmad. "Numerical simulation of Newtonian/non-Newtonian multiphase flows : deformation and collision of droplets." Doctoral thesis, Universitat Politècnica de Catalunya, 2019. http://hdl.handle.net/10803/667419.

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The complex nature of multiphase flows, particularly in the presence of non-Newtonian rheologies in the phases, limits the applicability of theoretical analysis of physical equations as well as setting up laboratory experiments. As a result, Computational Fluid Dynamics (CFD) techniques are essential tools to study these problems. Despite the advances in numerical simulation techniques in this field in the past decade, the applicability of these approaches are limited by challenges appearing in specific applications, and particular consideration must be taken into account for each of these pro

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22

Stocks, Marc Darren. "Geometric optimisation of heat transfer in channels using Newtonian and non-Newtonian fluids." Diss., University of Pretoria, 2012. http://hdl.handle.net/2263/33348.

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The continual advance in manufacturing processes has resulted in significantly more compact, high performance, devices. Consequently, heat extraction has become the limiting factor, and of primary concern. Therefore, a substantial amount of research has been done regarding high efficiency micro heat exchangers, employing novel working fluids. This dissertation numerically investigated the thermal behaviour of microchannel elements cooled by Newtonian and non-Newtonian fluids, with the objective of maximising thermal conductance subject to constraints. This was done, firstly, for a two-dimensi

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23

Smieszek, Marlene. "Structures and stability of Newtonian and non-Newtonian fluids in Taylor-Couette system /." Düsseldorf : VDI-Verl, 2008. http://d-nb.info/990760308/04.

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24

Anderson, Brian. "Development of a non-Newtonian latching device." Thesis, Manhattan, Kan. : Kansas State University, 2010. http://hdl.handle.net/2097/3855.

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25

Callahan, Thomas Patrick. "Non-Newtonian fluid injection into granular media." Thesis, Georgia Institute of Technology, 2011. http://hdl.handle.net/1853/39618.

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The process of fluid injection into granular media is relevant to a wide number of applications such as enhanced oil recovery, grouting, and the construction of permeable reactive barriers. The response of the subsurface is dependent on multiple factors such as in-situ stresses, fluid properties, flow rate, and formation type. Based on these conditions a variety of response mechanisms can be initiated ranging from simple porous infiltration to hydraulic fracturing. Currently, the mechanics of fluid injection into competent rock are well understood and can be sufficiently modeled using linear

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26

Lopez, Xavier. "Pore-scale modelling of non-Newtonian flow." Thesis, Imperial College London, 2004. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.415320.

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27

Ismail, Baharum. "Crossflow microfiltration of concentrated non-Newtonian slurries." Thesis, Loughborough University, 1996. https://dspace.lboro.ac.uk/2134/11787.

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Crossflow filtration of non-Newtonian slurries of magnesia and talc suspensions on micron-size membranes has been investigated. Three major membranes PTFE capillary, metal and ceramic tubes were employed and challenged by concentrated slurries more than 25 % by weight. Crossflow velocity, system pressure and slurry concentration are considered in relation to the possible deposit thickness and permeate flux behaviour. A thorough investigation of pressure drop in tubes of similar dimensions to the membranes has also been carried out in order to identify and develop an appropriate model. The expe

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28

Smith, Sarah Elizabeth. "Turbulent duct flow of non-Newtonian liquids." Thesis, University of Liverpool, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.399184.

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The turbulent flow of non-Newtonian fluids in straight ducts has been investigated. Specifically, the fully developed circular pipe flow, axisymmetric sudden expansion flow and fully developed square duct flow were studied. The pipe flow study analysed previous measurements of the mean velocity profiles and friction factor-Reynolds number characteristics of different non-Newtonian fluids in pipe fully developed pipe flows. An investigation of different nondimensional parameters permitted initial progress on developing a correlation between drag reduction and fluid rheology to be made. Comparis

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29

Wang, Yuli. "Capillarity and wetting of non-Newtonian droplets." Doctoral thesis, KTH, Mekanik, 2016. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-184146.

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Capillarity and dynamic wetting of non-Newtonian fluids are important in many natural and industrial processes, examples cover from a daily phenomenon as splashing of a cup of yogurt to advanced technologies such as additive manufacturing. The applicable non-Newtonian fluids are usually viscoelastic compounds of polymers and solvents. Previous experiments observed diverse interesting behaviors of a polymeric droplet on a wetted substrate or in a microfluidic device. However, our understanding of how viscoelasticity affects droplet dynamics remains very limited. This work intends to shed light

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30

Agarwal, Akshat. "Breakdown to turbulence in non-Newtonian flow." Thesis, Imperial College London, 2014. http://hdl.handle.net/10044/1/43851.

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Transition to turbulence in polymeric channel flow is investigated, with the FENE-P model used to characterize the viscoelastic behaviour of the flow. Simulations are performed to study transition through both the natural and bypass routes. In the linear growth regime of natural transition, differences in the growth rate of a TS wave are explained by appealing to the production of the perturbation energy budget. At high Weissenberg number, the growth rate is substantially lower in comparison to Newtonian flow. As a result, the transition process is prolonged. Upon the introduction of three dim

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31

Little, Stephen Nicholas. "The flow behaviour of non-Newtonian sludges." Thesis, University of Greenwich, 1998. http://gala.gre.ac.uk/6228/.

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A large body of data is analysed of the flow of concentrated sewage sludge through straight pipes. Mathematical models are obtained of the laminar and turbulent flow of each main category of sewage sludge. The sludges are modelled as time-independent, non-Newtonian relations between shear stress, rate of shearing strain, and solids concentration. Due to the inhomogeneity of sewage sludge, error analysis becomes pivotal to the data analysis, and options are examined for reducing the error of each model with one or more user-fitted parameters. Parameter estimation is discussed for viscous, time-

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32

Geurts, Kevin Richard. "Stochastic simulation of non-Newtonian flow fields /." Thesis, Connect to this title online; UW restricted, 1995. http://hdl.handle.net/1773/9821.

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33

Ireka, Ikenna Ebubechukwu. "Computational analysis of non-isothermal flow of non-Newtonian fluids." Doctoral thesis, University of Cape Town, 2015. http://hdl.handle.net/11427/15590.

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The dynamics of complex fluids under various conditions is a model problem in bio-fluidics and in process industries. We investigate a class of such fluids and flows under conditions of heat and/or mass transfer. Experiments have shown that under certain flow conditions, some complex fluids (e.g. worm-like micellar solutions and some polymeric fluids) exhibit flow instabilities such as the emergence of regions of different shear rates (shear bands) within the flow field. It has also been observed that the reacting mixture in reaction injection molding of polymeric foams undergoes self-expansio

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34

Dressler, Daniel. "An experimental investigation of Newtonian and non-Newtonian spray interaction with a moving surface." Thesis, University of British Columbia, 2006. http://hdl.handle.net/2429/71.

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As a logical extension of previous work conducted into viscoelastic atomization, initially motivated by the need to improve spray coating transfer efficiencies, an experimental investigation into the spray-surface interaction for a number of Newtonian and non-Newtonian substitute test liquids is presented. Three model elastic liquids of varying polymer molecular weight and three inelastic liquids of varying shear viscosity were sprayed upon a moving surface to isolate the effect of elasticity and shear viscosity, respectively, on spray impaction behavior. In addition, two liquids exhibiting s

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35

Singh, Brajesh Kumar. "Flow of Newtonian and non-Newtonian fluids in porous media, the viscous fingering instability." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2000. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape3/PQDD_0018/MQ49685.pdf.

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36

Amiri, Amin. "Buoyant miscible displacement flows of Newtonian and non-Newtonian fluids : stationary and oscillating geometries." Doctoral thesis, Université Laval, 2019. http://hdl.handle.net/20.500.11794/36974.

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Cette thèse vise l’étude des écoulement de déplacement de fluides miscibles à l’intérieur d’un long tuyau stationnaire vertical et d’un tuyau en mouvement. Concernant la géométrie des mouvements, le tuyau oscille comme un pendule inversé avec une fréquence maximale faible, c’est-à-dire, ˆf= 0.2(Hz) et une oscillation maximale de faible amplitude, soit 15 (◦) par rapport à l’axe du tuyau. Les écoulement de déplacement se produisent à un nombre de Péclet élevé et aux petits nombres d’Atwood. L’accent est mis sur les types de fluides et de géométries (tuyau fixe ou en mouvement). Les approches e

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37

Vayssière, Brandão Pedro <1993&gt. "Linear and nonlinear thermal instability of Newtonian and non-Newtonian fluid saturated porous media." Doctoral thesis, Alma Mater Studiorum - Università di Bologna, 2022. http://amsdottorato.unibo.it/10143/1/VayssiereBrandao_Pedro_PhD_Thesis.pdf.

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The present work aims to investigate the influence of different aspects, such as non-standard steady solutions, complex fluid rheologies and non-standard porous-channel geometries, on the stability of a Darcy-Bénard system. In order to do so, both linear and nonlinear stability theories are considered. A linear analysis focuses on studying the dynamics of the single disturbance wave present in the system, while its nonlinear counterpart takes into consideration the interactions among the single modes. The scope of the stability analysis is to obtain information regarding the transition from an

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38

Rostami, Behnam <1986&gt. "Experimental Analysis of Droplet Generation in Presence of Newtonian and non-Newtonian Flows within Microjunctions." Doctoral thesis, Alma Mater Studiorum - Università di Bologna, 2018. http://amsdottorato.unibo.it/8600/1/Thesis_final_Behnam%20Rostami.pdf.

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Microdroplets have attracted increasing interest among researchers due to the wide spread of promising technological applications such as biological analysis, cancer diagnosis, drug discovery and chemical reactions. With respect to traditional emulsion methods which are usually able to produce droplets with a broad size variation (polydispersed emulsions), microfluidic devices have been developed to produce monodispersed microdroplets with a controllable size. The diameter and size variation of droplets are controlled by a series of parameters, including the geometries and dimensions of the mi

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39

Mouzouri, Miloud. "Non-Newtonian Flow Modelling Through A Venturi Flume." Thesis, Toulouse, INPT, 2016. http://www.theses.fr/2016INPT0091.

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Lors d’une opération de forage, un certain nombre d’événements imprévus par rapport à l’écoulement du fluide de forage dans le puits, peuvent se produire assez rapidement. Des exemples de tels événements sont les afflux de pétrole ("kick") ainsi que les pertes de boue dans la formation. Un "kick" qui augmente en intensité peut entraîner, par ce que l’on nomme, un "blowout" (par exemple l’incident Deepwater Horizon en 2010). Les pertes et les gains sont habituellement détectés en contrôlant l’équilibre de la boue de forage dans le puits, en particulier en contrôlant le débit sortant du puits et

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40

Wielage, Kerstin. "Analysis of non-Newtonian and two-Phase flows." kostenfrei, 2005. http://deposit.ddb.de/cgi-bin/dokserv?idn=978191463.

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41

Wilson, Lynda M. Z. "Controllability of Non-Newtonian fluids under homogeneous flows." Thesis, Monterey, Calif. : Naval Postgraduate School, 2007. http://bosun.nps.edu/uhtbin/hyperion-image.exe/07Sep%5FWilson%5FLynda.pdf.

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Thesis (M.S. in Applied Mathematics)--Naval Postgraduate School, September 2007.<br>Thesis Advisor(s): Zhou, Hong. "September 2007." Description based on title screen as viewed on October 25, 2007. Includes bibliographical references (p. 47). Also available in print.

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42

Vongvuthipornchai, Somporn. "Well test analysis for non-Newtonian fluid flow /." Access abstract and link to full text, 1985. http://0-wwwlib.umi.com.library.utulsa.edu/dissertations/fullcit/8603796.

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43

Ketheeswaranathan, Nishanthi. "Rehological study of non-Newtonian fluid through microchannels." Thesis, University of Leeds, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.540775.

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44

Ngamaramvaranggul, V. D. "Numerical simulation of non-Newtonian free surface flows." Thesis, Swansea University, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.638326.

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Finite element numerical simulations are presented for two-dimensional creeping, planar and axisymmetric incompressible isothermal complex flows of both Newtonian and viscoelastic fluids. A number of constitutive equations are used to define fluid properties, including Newtonian, Oldroyd-B and Phan-Thien/Tanner (PTT) models. For viscoelastic flow, a modified semi-implicit Taylor-Galerkin method is presented with a consistent streamline upwind Petrov-Galerkin technique for the stress terms. Velocity gradient recovery is also employed. This multi-stage numerical solution algorithm implements a t

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45

DUTRA, EDUARDO STEIN SOARES. "DISPLACEMENT OF NON-NEWTONIAN LIQUIDS IN ECCENTRIC ANNULI." PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO, 2005. http://www.maxwell.vrac.puc-rio.br/Busca_etds.php?strSecao=resultado&nrSeq=6947@1.

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PETRÓLEO BRASILEIRO S. A.<br>Após a perfuração de poços de petróleo, a lama utilizada na remoção de cascalho, lubrificação e resfriamento da broca deve ser removida e substituída por uma mistura de cimento. Essa substituição se dá pelo deslocamento de um fluido por outro no espaço anular entre a formação rochosa e a coluna de completação ou revestimento. A mistura de cimento tem a função de garantir a estabilidade estrutural do poço evitando danos ambientais e prejuízos econômicos. Para melhores resultados do processo de cimentação, utilizam-se fluidos intermediários, também chamados de

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46

BAZZI, MARISA SCHMIDT. "BREAKUP DYNAMICS OF NON-NEWTONIAN THIN LIQUID SHEETS." PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO, 2018. http://www.maxwell.vrac.puc-rio.br/Busca_etds.php?strSecao=resultado&nrSeq=34574@1.

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PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO<br>COORDENAÇÃO DE APERFEIÇOAMENTO DO PESSOAL DE ENSINO SUPERIOR<br>FUNDAÇÃO DE APOIO À PESQUISA DO ESTADO DO RIO DE JANEIRO<br>PROGRAMA DE EXCELENCIA ACADEMICA<br>BOLSA NOTA 10<br>Filmes finos de líquidos estão presentes em uma gama de aplicações industriais, como processos de atomização e revestimento de substrato. O processo de quebra pode ser divido em duas etapas: o estágio de ruptura, e o estágio de retração. O primeiro, movido pelas forças de van der Waals, ocorre quando uma pequena perturbação cresce e provoca o aparecimento de um peque

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47

Haldenwang, Rainer. "Flow of non-newtonian fluids in open channels." Thesis, Cape Technikon, 2003. http://hdl.handle.net/20.500.11838/1042.

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Dissertation (DTech (Civil Engineering))--Cape Technikon, Cape Town, 2003<br>Flume design for homogeneous non-Newtonian fluids is problematic and not much research has been conducted in this field. This application is industrially important in mining where slurries have to be transported to processing or disposal sites at higher concentrations because water is becoming a scarce and expensive commodity. This thesis addresses the problem of flume design and develops predictive models for the laminar, transitional and turbulent flow behaviour of non-Newtonian fluids in rectangular open chann

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48

Kabwe, Aime Mume. "Non-Newtonian loss coefficients for Saunders diaphragm valves." Thesis, Cape Peninsula University of Technology, 2009. http://hdl.handle.net/20.500.11838/914.

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Dissertation submitted in fulfilment of requirements for the degree Master Technology: Chemical Engineering in the FACULTY OF ENGINEERING at the CAPE PENINSULA UNIVERSITY OF TECHNOLOGY, 2009<br>The prediction of the energy losses when designing pipeline and pumping systems requires accurate loss coefficient data. But the loss coefficient data found in the open literature was not adequate for predicting the loss coefficient for Saunders straight-through diaphragm valves. As more accurate loss coefficient data to enable more efficient pipeline designs are scarce in the open literature, it is pro

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49

Berti, Stefano. "Non-Newtonian turbulence : viscoelastic fluids and binary mixtures." Nice, 2006. http://www.theses.fr/2006NICE4079.

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Cette thèse présente une étude théorique et numérique de la turbulence dans les fluides non-Newtoniens, dont la dynamique peut être modélisée en termes du transport de champs actifs et c’est un sujet d’intérêt général pour la physique des fluides complexes. Leur rhéologie particulière les rend, en outre, intéressants pour des applications en ingénierie. La plus grande partie du travail regarde les solutions diluées de polymères. Deux aspects sont considérés : la statistique aux petites échelles, pour des élasticités modérées dans un régime de turbulence développée ; la déstabilisation d’un éco

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50

Kabwe, Aime Mume. "Non-newtonian loss coefficient for Saunders diaphragm valves /." [S.l. : s.n.], 2009. http://dk.cput.ac.za/cgi/viewcontent.cgi?article=1008&context=td_cput.

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