- About
-
The Global ETD Search service is a free service for researchers
to find electronic theses and dissertations. This service is
provided by the
Networked Digital Library of Theses and Dissertations.
Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
Search results
Showing 131 to 140 of 1441 (0.033 seconds)Spelling suggestions: "subject:"hydrodynamic""
| 131 |
Solitons and wave propagation in hydrodynamical and optical mediaMak, Chun-chung., 麥振忠. January 2004 (has links)
published_or_final_version / abstract / toc / Mechanical Engineering / Master / Master of Philosophy
|
| 132 |
Numerical methods in wave loading of large offshore structures周奮鵬, Chau, Fun-pang. January 1985 (has links)
published_or_final_version / Mechanical Engineering / Master / Master of Philosophy
|
| 133 |
Hydrodynamic behaviour of biological aggregates: settling and coagulation with small particlesYuan, Yuan, 袁媛 January 2000 (has links)
published_or_final_version / Civil Engineering / Master / Master of Philosophy
|
| 134 |
THE TWO-DIMENSIONAL JET UNDER GRAVITY FROM AN APERTURE IN THE LOWER OF TWO HORIZONTAL PLANES WHICH BOUND A LIQUIDConway, William Edward, 1938- January 1965 (has links)
No description available.
|
| 135 |
FORCES AND MOMENTS ON FINITE SPAN HYDROFOILS IN ACCELERATED MOTIONZucker, Robert Diefendorf, 1925- January 1966 (has links)
No description available.
|
| 136 |
Drying of slurries in spouted bedsSchneider, Torsten January 1987 (has links)
No description available.
|
| 137 |
The behavior of colloidal dispersions in poiseuille flow.Vadas, Elizabeth Büchler January 1972 (has links)
No description available.
|
| 138 |
Bench-scale two-dimensional fluidized bed hydrodynamics and struvite growth studiesQu, Xiaocao 05 1900 (has links)
A bench-scale, two-dimensional multi-compartmentalized fluidized reactor was designed and studies of hydrodynamic behavior of fluidization of struvite pellets were performed. Also size growth distribution tests were analyzed qualitatively.
The study validated a previously-proposed theory, concerning the relationship between dynamic pressure drop and upflow velocity as well the experimental protocol to determine the minimum fluidization velocity. Findings indicated that the mixture of two-sized particles would behave rather independently of each other, before the bed expansion. It was suggested that bed height measurement could be another promising method to pinpoint minimum fluidization velocity as there is a sharp bed surface "waking episode" during the process of a packed bed being gradually fluidized.
Bed expansion equations for the prediction of void fraction as a function of superficial upflow velocity or vice versa, have been established for 4 groups of monosize particles, as well as two mixtures of two-sized particles. The equation constants did not agree well with previously established ones. The two layers of segregated mixture bed had congruent linear relationships between the logarithmic void fraction and logarithmic upflow velocity. It was found that a mixture does not always go through segregation, but only when the size difference is large enough.
Size growth distribution tests were performed under different hydrodynamic configurations as well as seeding conditions. Conclusions can be made that a bed with uniformly- distributed particle void fractions and higher mixing energy input (upflow velocity), normally has better performance of struvite growth in size.
|
| 139 |
A mathematical model for magma-hydrothermal systems in the oceanic crustSalstrand, Daniel Koewing 12 1900 (has links)
No description available.
|
| 140 |
Hydrodynamic and electric particle interactions in suspensionsArp, Paul Alexander January 1975 (has links)
No description available.
|
Page generated in 0.0391 seconds