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WALL JETS ON CURVED SURFACESCoxon, Moran, 1930- January 1971 (has links)
No description available.
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HEAT AND MOMENTUM TRANSFER BETWEEN PARALLEL POROUS PLATESDoughty, John Robert, 1936- January 1971 (has links)
No description available.
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ENTRY FLOW IN A CIRCULAR TUBEBates, John Anthony, 1935- January 1972 (has links)
No description available.
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Laminar flow in porous ductsWhite, Frank Mangrem 05 1900 (has links)
No description available.
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Laminar flow in a uniformly porous channelBarfield, Bobby Fred 08 1900 (has links)
No description available.
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Laminar, steady and unsteady flow over inclined plates in two and three dimensions /Hytopoulos, Evangelos, January 1990 (has links)
Thesis (M.S.)--Virginia Polytechnic Institute and State University, 1990. / Vita. Abstract. Includes bibliographical references (leaves 120-122). Also available via the Internet.
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Energy losses in bends of large curvature ratiosel-Kouh, Abdel Fattah, January 1957 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1957. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 94-97).
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Illustrations of mixing in laminar flowNg, Kwok Yuk. January 1979 (has links)
Thesis (M.S.)--University of Wisconsin--Madison. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 149-150).
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Disturbed laminar pipe flowMajumdar, Hirendra. January 1964 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1964. / eContent provider-neutral record in process. Description based on print version record. Bibliography: l. 59-60.
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Numerical solution for stratified laminar flow of two immiscible Newtonian liquids in a circular pipeGemmell, Alan Robert January 1961 (has links)
Numerical solutions of the velocity profiles for laminar, stratified flow of two immiscible, Newtonian liquids in a circular pipe were determined for viscosity ratios of 1, 10, 100 and 1000 at various interface positions. These results were used to calculate the theoretical volumetric flow rate enhancement factors, power reduction factors and hold-up ratios, which for laminar flow depend only upon the viscosity ratio and the interface position. The maximum volumetric flow rate enhancement factors and maximum power reduction factors, and the corresponding input volume ratios, were determined. Dimensionless quantities were used, making the results applicable to any pipe diameter, any liquid viscosities and any pressure gradient, providing laminar flow of both phases prevails.
The theoretical results were compared to the experimental results of Russell, Hodgson and Govier for horizontal cocurrent flow of a mineral oil and water in a circular pipe. As expected, the two sets of results differed considerably in the region of turbulent water flow. As turbulence decreased however, the difference decreased, until in the laminar region very good agreement between the theoretical and experimental results was obtained. / Applied Science, Faculty of / Chemical and Biological Engineering, Department of / Graduate
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