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Laminar Newtonian and non-Newtonian converging flow in conical sectionsSutterby, John LLoyd, January 1964 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1964. / Typescript. Includes abstract (leaf ii) and summary (leaves xxi-xxv). Vita. Description based on print version record. Includes bibliographical references (leaves G-1-G-9).
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Phenomonological behaviour of particles in Newtonian and non-Newtonian liquids.Bartram, Eric. January 1973 (has links)
No description available.
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Rheological characterization of high density polyethylene with processing aids in capillary flow and its implications in a non-isothermal annular flow processNguyen, Khanh Phuong 08 1900 (has links)
No description available.
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Analysis of non-Newtonian effects in separated blood flow regionsDavis, Paul H. 12 1900 (has links)
No description available.
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Analysis of polymer flows in the three dimensional extrusion diesYu, Zuwei. January 1994 (has links)
Thesis (M.S.)--Ohio University, November, 1994. / Title from PDF t.p.
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Direct simulations of spherical particle motion in non-Newtonian liquidsPrashant. January 2009 (has links)
Thesis (M. Sc.)--University of Alberta, 2009. / Title from PDF file main screen (viewed on Oct. 21, 2009). "A thesis submitted to the Faculty of Graduate Studies and Research in partial fulfillment of the requirements for the degree of Master of Science in Chemical Engineering, Department of Chemical and Materials Engineering, University of Alberta." Includes bibliographical references.
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Direct simulations of spherical particle motion in non-Newtonian liquidsPrashant. January 2009 (has links)
Thesis (M. Sc.)--University of Alberta, 2009. / Title from PDF file main screen (viewed on Oct. 21, 2009). "A thesis submitted to the Faculty of Graduate Studies and Research in partial fulfillment of the requirements for the degree of Master of Science in Chemical Engineering, Department of Chemical and Materials Engineering, University of Alberta." Includes bibliographical references.
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The viscosity of suspensions of rigid spherical particles in viscoelastic fluidsRiddle, Michael Joseph. January 1977 (has links)
Thesis--Wisconsin. / Vita. Includes bibliographical references (leaves E1-E4).
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Flow of non-Newtonian fluids in annuliFredrickson, Arnold G. January 1959 (has links)
Thesis (Ph. D.)--University of Wisconsin, 1959. / eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 13-1-13-9).
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Time effects in evolution of structure and rheology of highly concentrated emulsionsKharatiyan, Ellina January 2005 (has links)
Thesis (DTech (Chemical Engineering))--Cape Peninsula University of Technology, 2005. / The subject of this study is highly concentrated emulsion explosive (HCEE). These emulsions
are dispersions of an aqueous phase (up to 90 v-%) in an oil phase. The dispersed droplets
consist of an aqueous solution of nitrate salts, which is supersaturated at room temperature,
comprising less than 20% of water by mass. Compounds of this kind are thermodynamically
unstable and their instability is related to the coarsening of emulsion (coalescence) and phase
transition (crystallization) of dispersed phase. However it is demonstrated that the dominating
mechanism is slow crystallization inside the super-cooled droplets. The main goal of this
thesis is a phenomenological study of the dependence of structural parameters, such as droplet
size and volume fraction, as well as the ageing processes, on the rheological properties of
these emulsions.
The results of the measurements include the flow and viscoelastic properties of the materials.
The rheological parameters are correlated with the kinetics of structural changes during
ageing, as a function of emulsion formulation. The emulsions under study are non-Newtonian liquids. Experiments in shear rate sweep mode
demonstrate that the upward and downward branches of the flow curves coincide above some
specific shear rate value. The upward experiments show the existence of a low shear
Newtonian asymptote, while the effect of yielding is observed in the downward curve. Wall
slip is investigated and shown to be negligible.
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