I visualized the flash-boiling atomization of liquid jets released into a low pressure environment at frame rates of up to five million frames per second. Such a high temporal resolution allowed us to observe for the first time the bubble expansion mechanism that atomizes the jet. To visualize the dynamics in detail, I focused closely to the outflow of the nozzle using a long distance microscope objective. I documented an abrupt transition from a laminar to a fully external flashing jet by systematically reducing the ambient pressure. I performed experiments with different volatile liquids and using nozzles with different inner diameters. The inner diameters of the nozzles varied from 30 to 480 µm. Perfluorohexane (PFnH) was our main working fluid, but also methanol, ethanol and 1-bromopropane were tested. Surprisingly, minimum intensity profiles revealed spray angles close to θs ~360°, meaning drops are ejected in all directions. Also, I measured speeds of bubble expansion up to 140 m/s. That is 45 times faster than the upper bound for inertial growth speed in complete vacuum from the Rayleigh-Plesset equation. I also calculated the trajectories of the ejected droplets as well as the drop speed distribution using particle tracking. I expect that our results bring new insight into the flash-boiling atomization mechanism.

Thesis (B.S.)--Massachusetts Institute of Technology, Dept. of Nuclear Engineering, 1980. / MICROFICHE COPY AVAILABLE IN ARCHIVES AND SCIENCE. / Includes bibliographical references. / by Paul William Bordley. / B.S.

No description available.

No description available.

A suboptimal controller has been developed for a Boiling Water Reactor Nuclear Power Plant, using the DARE P Continuous Simulation Language, which was developed in the Electrical Engineering Department at the University of Arizona. A set of 48 nonlinear first-order differential equations and a large number of algebraic equations has been linearized about the equilibrium state. Using partitioning, the linearized equations were transformed into a block triangular form. The concept of optimal control and a square performance index reflecting the desired plant behavior have been applied on the slow subsystem to develop a suboptimal controller. The obtained feedback law is shown by simulation to be able to compensate for a variety of plant disturbances. A large variety of responses can be obtained by changing the weighting matrices. The control is basically a regulator approach to speed up response during load demand changes. Several simulations are included to demonstrate the control performance. The variables to be controlled have mainly been the average neutron density and the average coolant temperature. Simplifications have been suggested, thus obtaining considerable savings in the computations and ease in design.

Recent studies have shown that thermophotovoltaic (TPV) technology is a promising source of high power density generation. Enhanced TPV systems can theoretically provide power densities of up to 100 W/cm2. The inherent ineffiencies in the system dictate that up to 90% of that energy is not converted to electrical power, and must be removed as waste heat to ensure that the components are maintained at a reasonable operating temperature. The present study addresses this issue by investigating the suitability of using spray cooling techniques to remove heat generated by power densities of up to 100 W/cm2. A simple, scaleable experiment was designed using low-cost commercially available components to study the effects that spray mass flux and droplet size have on the heat removal capacity of the system. A series of nozzles were used so that mass flux and droplet size could be studied independently, giving high resolution to the data so that predictive correlations could be developed over the range of parameters varied in the study. / US Naval Reserve (USNR) author.

Two-phase flows with or without phase change are present in terrestrial and space applications like thermal control of satellites, propellant supply for launchers, and waste water treatment for space exploration missions. Flow boiling experiment with HFE7000 were conducted in a heated tube in vertical upward flow on ground and in microgravity conditions to collect data on flow patterns, pressure drops, heat transfers, void fraction. Void fraction measurements allowed to measure mean gas velocity and the liquid film thickness in annular flow. In microgravity condition, the liquid film thickness and the interfacial shear stress are significantly lower than in normal gravity. A detail analysis of the film structure was performed by image processing. The impact of gravity and liquid and vapour superficial velocities on the disturbance waves velocities and frequencies was investigated. Two different measurement techniques were used and compared to determine the heat transfer coefficient. For quality values greater than 0.2, HTC is not sensitive to gravity and is in good agreement with classical correlations of the literature. For qualities smaller than 0.1, in the subcooled nucleate boiling regime HTC is significantly smaller in microgravityconditions.

Electrohydrodynamic (EHD) phenomena involve the interaction between electrical and flow fields in a dielectric fluid medium. In EHD conduction, the electric field causes an imbalance in the dissociation-recombination reaction of neutral electrolytic species, generating free space charges which are redistributed to the vicinity of the electrodes. Proper asymmetric design of the electrodes generates net axial flow motion, pumping the fluid. EHD conduction pumps can be used as the sole driving mechanism for small-scale heat transport systems because they have a simple electrode design, which allows them to be fabricated in exceedingly compact form (down to micro-scale). EHD conduction is also an effective technique to pump a thin liquid film. However, before specific applications in terrestrial and micro-gravity thermal management can be developed, a better understanding of the interaction between electrical and flow fields with and without phase-change and in the presence and absence of gravity is needed. With the above motivation in mind, detailed experimental work in EHD conduction-driven single- and two-phase flow is carried out. Two major experiments are conducted both terrestrially and on board a variable gravity parabolic flight. Fundamental behavior and performance evaluation of these electrically driven heat transport systems in the respective environments are studied. The first major experiment involves a meso-scale, single-phase liquid EHD conduction pump which is used to drive a heat transport system in the presence and absence of gravity. The terrestrial results include fundamental observations of the interaction between two-phase flow pressure drop and EHD pump net pressure generation in meso-scale and short-term/long-term, single- and two-phase flow performance evaluation. The parabolic flight results show operation of a meso-scale EHD conduction-driven heat transport system for the first time in microgravity. The second major experiment involves liquid film flow boiling driven by EHD conduction in the presence and absence of gravity. The terrestrial experiments investigate electro-wetting of the boiling surface by EHD conduction pumping of liquid film, resulting in enhanced heat transfer. Further research to analyze the effects on the entire liquid film flow boiling regime is conducted through experiments involving nanofiber-enhanced heater surfaces and dielectrophoretic force. In the absence of gravity, the EHD-driven liquid film flow boiling process is studied for the first time and valuable new insights are gained. It is shown that the process can be sustained in micro-gravity by EHD conduction and this lays the foundation for future experimental research in electrically driven liquid film flow boiling. The understanding gained from these experiments also provides the framework for unique and novel heat transport systems for a wide range of applications in different scales in terrestrial and microgravity conditions.

Thesis. 1975. Sc.D.--Massachusetts Institute of Technology. Dept. of Mechanical Engineering. / Vita. / Bibliography: leaves 82-84. / Sc.D.

Thesis. 1978. Sc.D.--Massachusetts Institute of Technology. Dept. of Chemical Engineering. / MICROFICHE COPY AVAILABLE IN ARCHIVES AND SCIENCE. / Vita. / Bibliography: leaves 421-426. / by Jaime A. Valencia-Chávez. / Sc.D.