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Fluidelastic Instability of Finned Tube Bundles in Normal and Parallel Triangular ArraysWang, Jing 20 November 2017 (has links)
Experimental study was conducted to investigate fluidelastic instability in finned tube bundles with normal and parallel triangular arrays. Three arrays of each geometry type were studied experimentally: two arrays with serrated, helically wound finned tubes of different fin densities, and a bare tube array with the same base diameter as the finned tubes. The finned tubes under consideration were commercial finned tubes typically used in the fossil and process industries. For the purpose of the present investigation, the concept of "effective diameter" of a finned tube, as used to predict the vortex shedding, was used to compare the finned tube results with the existing bare tube world data and some theoretical predictions for fluidelastic instability. The finned tube arrays in this study have the same tube pitch and have been scaled to have the same mass ratio and tuned to have the same natural frequency. A low speed wind tunnel, Betz micro manometer and HP 35670a dynamic signal analyzer were employed to conduct the experiments. Experimental results for the triangular arrays show that the fin's structure strongly influences the fluidelastic stability of finned tube bundles and the fin pitch is demonstrated to reduce the difference in the fluidelastic instability between the tube arrangements as the fin density increases. The results also suggest that there might be an optimum fin pitch value at which the threshold reduced velocity for a finned tube array is much higher than the one for its corresponding bare tube array, due to the influence of fin geometry. In the appendix, an analytical model produces a new correlation of critical reduced velocity against mass damping parameter to predict the fluidelastic instability of tube bundles. Its predictions are in reasonable agreement with the experimental data. Since negative damping is one of the mechanisms of fluidelastic instability of a tube array, "Lift effect" was applied to explain the negative damping in an inviscid flow. An experiment is suggested to test the relationship between the pitch flow velocity and a tube velocity dependent "lift effect". Accordingly, two duct structure designs are suggested which may alleviate the negative damping by using the energy of oncoming flow to reduce the "lift effect" on the tubes. / Thesis / Master of Applied Science (MASc)
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Numerically Modeling the Flow and Friction Within a Helically-Finned TubeShuster, James Louis 24 May 2010 (has links)
No description available.
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Effect of vapor velocity during condensation on horizontal finned tubesHopkins, Charles Louis III 12 1900 (has links)
Approved for public release; distribution is unlimited / Heat-transfer measurements were made for condensation of
R-113 and steam on a smooth tube and on three finned tubes
with rectangular shape fins. These tubes had a fin height
and width of 1.0 mm and spacings of 0.25, 1.5, and 4.0 mm
(tubes A, B, and C respectively) . Data were taken by
increasing the vapor velocity from 0.4 to 1.9 m/s for R-113
and 4.8 to 31.3 m/s for steam. For both fluids, the
improvement of the condensing heat-transfer coefficient with
vapor velocity was smaller for the finned tubes than for the
smooth tube. For R-113, the smooth tube experienced a 32
percent improvement with vapor velocity, where the finned
tubes (tubes A, B and C respectively) experienced
improvements of only 0, 5 and 10 percent. For steam, the
smooth tube experienced a 62 percent improvement, whereas
the finned tubes (tubes A, B, and C respectively)
experienced improvements of only 31, 11, and 9 percent.
These test results show that, although finned tubes can
provide significant heat transfer enhancement over smooth
tubes at low vapor velocities, the degree of enhancement
becomes smaller as vapor velocity increases. / CBT-8603582 (NSF) / http://archive.org/details/effectofvaporvel00hopk / National Science Foundation / Lieutenant Commander, United States Navy
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Pool boiling on nano-finned surfacesSriraman, Sharan Ram 15 May 2009 (has links)
The effect of nano-structured surfaces on pool boiling heat transfer is explored in this
study. Experiments are conducted in a cubical test chamber containing fluoroinert
coolant (PF5060, Manufacturer: 3M Co.) as the working fluid. Pool boiling experiments
are conducted for saturation and subcooled conditions. Three different types of ordered
nano-structured surfaces are fabricated using Step and flash imprint lithography on
silicon substrates followed by Reactive Ion Etching (RIE) or Deep Reactive Ion Etching
(DRIE). These nano-structures consist of a square array of cylindrical nanofins with a
longitudinal pitch of 1 mm, transverse pitch of 0.9 mm and fixed (uniform) heights
ranging from 15 nm – 650 nm for each substrate. The contact angle of de-ionized water
on the substrates is measured before and after the boiling experiments. The contact-angle
is observed to increase with the height of the nano-fins. Contact angle variation is also
observed before and after the pool boiling experiments.
The pool boiling curves for the nano-structured silicon surfaces are compared with that
of atomically smooth single-crystal silicon (bare) surfaces. Data processing is performed
to estimate the heat flux through the projected area (plan area) for the nano-patterned
zone as well as the heat flux through the total nano-patterned area, which includes the surface area of the fins. Maximum heat flux (MHF) is enhanced by ~120 % for the nanofin
surfaces compared to bare (smooth) surfaces, under saturation condition. The pool
boiling heat flux data for the three nano-structured surfaces progressively overlap with
each other in the vicinity of the MHF condition. Based on the experimental data several
micro/nano-scale transport mechanisms responsible for heat flux enhancements are
identified, which include: “microlayer” disruption or enhancement, enhancement of
active nucleation site density, enlargement of cold spots and enhancement of contact
angle which affects the vapor bubble departure frequency.
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Pool boiling on nano-finned surfacesSriraman, Sharan Ram 10 October 2008 (has links)
The effect of nano-structured surfaces on pool boiling heat transfer is explored in this
study. Experiments are conducted in a cubical test chamber containing fluoroinert
coolant (PF5060, Manufacturer: 3M Co.) as the working fluid. Pool boiling experiments
are conducted for saturation and subcooled conditions. Three different types of ordered
nano-structured surfaces are fabricated using Step and flash imprint lithography on
silicon substrates followed by Reactive Ion Etching (RIE) or Deep Reactive Ion Etching
(DRIE). These nano-structures consist of a square array of cylindrical nanofins with a
longitudinal pitch of 1 mm, transverse pitch of 0.9 mm and fixed (uniform) heights
ranging from 15 nm - 650 nm for each substrate. The contact angle of de-ionized water
on the substrates is measured before and after the boiling experiments. The contact-angle
is observed to increase with the height of the nano-fins. Contact angle variation is also
observed before and after the pool boiling experiments.
The pool boiling curves for the nano-structured silicon surfaces are compared with that
of atomically smooth single-crystal silicon (bare) surfaces. Data processing is performed
to estimate the heat flux through the projected area (plan area) for the nano-patterned
zone as well as the heat flux through the total nano-patterned area, which includes the surface area of the fins. Maximum heat flux (MHF) is enhanced by ~120 % for the nanofin
surfaces compared to bare (smooth) surfaces, under saturation condition. The pool
boiling heat flux data for the three nano-structured surfaces progressively overlap with
each other in the vicinity of the MHF condition. Based on the experimental data several
micro/nano-scale transport mechanisms responsible for heat flux enhancements are
identified, which include: "microlayer" disruption or enhancement, enhancement of
active nucleation site density, enlargement of cold spots and enhancement of contact
angle which affects the vapor bubble departure frequency.
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The “Fish-Specific” Hox Cluster Duplication Is Coincident with the Origin of TeleostsCrow, Karen D., Stadler, Peter F., Lynch, Vincent J., Amemiya, Chris, Wagner, Günter P. 10 December 2018 (has links)
The Hox gene complement of zebrafish, medaka, and fugu differs from that of other gnathostome vertebrates. These fishes have seven to eight Hox clusters compared to the four Hox clusters described in sarcopterygians and shark. The clusters in different teleost lineages are orthologous, implying that a “fish-specific” Hox cluster duplication has occurred in the stem lineage leading to the most recent common ancestor of zebrafish and fugu. The timing of this event, however, is unknown. To address this question, we sequenced four Hox genes from taxa representing basal actinopterygian and teleost lineages and compared them to known sequences from shark, coelacanth, zebrafish, and other teleosts. The resulting gene genealogies suggest that the fish-specific Hox cluster duplication occurred coincident with the origin of crown group teleosts. In addition, we obtained evidence for an independent Hox cluster duplication in the sturgeon lineage (Acipenseriformes). Finally, results from HoxA11 suggest that duplicated Hox genes have experienced diversifying selection immediately after the duplication event. Taken together, these results support the notion that the duplicated Hox genes of teleosts were causally relevant to adaptive evolution during the initial teleost radiation.
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Study of Laminar Flow Forced Convection Heat Transfer Behavior of a Phase Change Material FluidRavi, Gurunarayana 14 January 2010 (has links)
The heat transfer behavior of phase change material fluid under laminar flow conditions in circular tubes and internally longitudinal finned tubes are presented in this study. Two types of boundary conditions, including uniform axial heat flux with constant peripheral temperature and uniform axial and peripheral temperature, were considered in the case of circular tubes. An effective specific heat technique was used to model the phase change process assuming a hydrodynamically fully-developed flow at the entrance of the tube. Results were also obtained for the phase change process under hydro dynamically and thermally fully developed conditions. In case of a smooth circular tube with phase change material (PCM) fluid, results of Nusselt number were obtained by varying the bulk Stefan number. The Nusselt number results were found to be strongly dependent on the Stefan number. In the case of a finned tube two types of boundary conditions were studied. The first boundary condition had a uniform axial heat flux along the axis of the tube with a variable temperature on the peripheral surface of the tube. The second boundary condition had a constant temperature on the outer surface of the tube. The effective specific heat technique was again implemented to analyze the phase change process under both the boundary conditions. The Nusselt number was determined for a tube with two fins with different fin height ratios and fin thermal conductivity values. It was determined that the Nusselt number was strongly dependent on the Stefan number, fin thermal conductivity value, and height of the fins. It was also observed that for a constant heat axial flux boundary condition with peripherally varying temperature, the phase change slurry with the internally finned tube performed better than the one without fins. A similar trend was observed during the phase change process with internal fins under the constant wall temperature boundary condition.
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Study of Laminar Flow Forced Convection Heat Transfer Behavior of a Phase Change Material FluidRavi, Gurunarayana 14 January 2010 (has links)
The heat transfer behavior of phase change material fluid under laminar flow conditions in circular tubes and internally longitudinal finned tubes are presented in this study. Two types of boundary conditions, including uniform axial heat flux with constant peripheral temperature and uniform axial and peripheral temperature, were considered in the case of circular tubes. An effective specific heat technique was used to model the phase change process assuming a hydrodynamically fully-developed flow at the entrance of the tube. Results were also obtained for the phase change process under hydro dynamically and thermally fully developed conditions. In case of a smooth circular tube with phase change material (PCM) fluid, results of Nusselt number were obtained by varying the bulk Stefan number. The Nusselt number results were found to be strongly dependent on the Stefan number. In the case of a finned tube two types of boundary conditions were studied. The first boundary condition had a uniform axial heat flux along the axis of the tube with a variable temperature on the peripheral surface of the tube. The second boundary condition had a constant temperature on the outer surface of the tube. The effective specific heat technique was again implemented to analyze the phase change process under both the boundary conditions. The Nusselt number was determined for a tube with two fins with different fin height ratios and fin thermal conductivity values. It was determined that the Nusselt number was strongly dependent on the Stefan number, fin thermal conductivity value, and height of the fins. It was also observed that for a constant heat axial flux boundary condition with peripherally varying temperature, the phase change slurry with the internally finned tube performed better than the one without fins. A similar trend was observed during the phase change process with internal fins under the constant wall temperature boundary condition.
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Thermo-fluid modelling of electrical generator frames under forced convection in an oscillating water column environmentAhmed, Nisaar January 2018 (has links)
This PhD involved computational fluid dynamic simulations of finned generators cooling under forced convection in an oscillating water column environment. Various design changes to the upstream Wells turbine and its effect on the consequent cooling of the generator were investigated. Simulations were run in steady-state to obtain an initial condition, thereafter, unsteady simulations revealed a steadying of heat transfer over the course of multiple blade rotation cycles. This justified the use of steady-state for the remaining simulations over a range of flow coefficients. The results revealed that the heat transfer from the generator increased for tighter blade tip clearances, thicker blade profiles and greater turbine solidity. The heat transfer was found to increase with rising flow rate coefficient, which was adjusted by increasing the inlet velocity whilst maintaining the angular velocity of the turbine at a constant 2000 RPM. Additionally, the variation of turbine angular velocity at a fixed flow rate coefficient was investigated, the heat transfer was also found to increase with angular velocity, albeit by a far lesser extent. The inclusion of the Wells turbine upstream of the generator was investigated initially and was found to increase heat transfer due to the resulting impingement of airflow across the generator. In all design scenarios in which the heat transfer increases, there is also an observed increase in the mass flow rate of air, radially, towards the generator.
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Evolution of the Neuropeptide Y System in Vertebrates with Focus on FishesLarsson, Tomas January 2007 (has links)
<p>Gene families in vertebrates often contain more dulicates (paralogs) than in invertebrates. This has been attributed to genome duplications, i.e., tetraploidizations. Two of the gene families that have expanded in vertebrate evolution are the neuropeptide Y (NPY) family of peptides and the neuropeptide Y receptors (NPYR) that are involved in many brain functions including appetite regulation.</p><p>Two NPYR genes, Y2 and Y7, were cloned in the rainbow trout. Although they arose from a common ancestral gene in early vertebrate evolution, their ligand-binding properties are very similar. Two NPYR genes were cloned in the coelacanth <i>Latimeria chalumnae</i> and found to be orthologs of Y5 and Y6 discovered in mammals.</p><p>Analyses of gene families close to the NPYR genes in the pufferfishes <i>T. nigroviridis</i> and <i>T. rubripes</i> showed that at least 25 additional gene families had an evolutionary history similar to the NPYR family, thereby providing evidence for fish specific-duplications of these chromosomes. Cloning and phylogenetic analysis of 22 NPYR gene fragments from several ray-finned fishes showed that basal species seem to have the same repertoire as tetrapods. Despite the tetraploidization in the teleost fish lineage, many teleosts seem to have fever genes than the gnathostome ancestor due to gene loss. Only one duplicate seems to have survived.</p><p>The NPY peptide family was found to have expanded in the teleost tetraploidization with duplicates of both NPY and PYY (peptide YY) in some teleosts. Fourteen neighboring gene families were found to have evolved in a similar manner as the NPY-family genes. Positional information fascilitated orthology assignment of peptide genes in teleost fishes and allowed correction of previously misidentified genes.</p><p>In summary, the evolutionary history of the NPY and NPYR gene families involve large-scale duplication events coinciding with the proposed tetraploidizations. The appearance of new genes in early vertebrates and in teleost fishes probably had important implications for the evolution of new functions in this system.</p>
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