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Heated-plate experiment

The number of the flies that can be paced at one time is limited by electrode size and the experimenter s experience usually less than ten flies per session. To maintain a constant temperature throughout the experiment, a heating plate (Brook Industries, Lake Villa, IL) that can rest on the microscope stage is used (Fig. la). [Pg.247]

Extensive experiments have been conducted by Fujii and Imura [44] for heated plates in water at various angels of inclination. The angle which the plate makes with the vertical is designated 6, with positive angles indicating that the heater... [Pg.343]

Pure crossflow is found in flat plate heat exchangers, as indicated by Fig. 1.22. The temperatures of both fluids also change perpendicular to the flow direction. This is schematically shown in Fig. 1.23. Each fluid element that flows in a crossflow heat exchanger experiences its own temperature change, from the entry temperature which is the same for all particles to its individual exit temperature. Crossflow is often applied in a shell-and-tube heat exchanger when one of the fluids is gaseous. The gas flows around the rows of tubes crosswise to the tube axis. The other fluid, normally a liquid, flows inside the tubes. The addition of... [Pg.42]

Forced and free flow can, depending on the direction of the inertia and buoyancy forces, either mutually stimulate or dampen each other. In a forced flow overlapping a free flow, the heat and mass transfer can either be improved or inhibited. As an example of this we will look at a heated plate, Fig. 3.51. A free flow in the upwards direction develops, which can be strengthened Fig. 3.51a, or weakened, Fig. 3.51b, by a forced flow generated by a blower. Experiments have shown that the heat transfer coefficient can be calculated well by using equations of the form... [Pg.387]

The temperature is registered by an iron-constantan thermocouple located in the metal support plate 4. The instrument gives the opportunity of measuring the intensity of emitted light vs. temperature from room temperature up to 300°C. Izothermal as well as various heating rate experiments can be carried out with the precision of the temperature control of il°C. [Pg.389]

Equation for C,. A number of experiments at different Prandtl numbers (mostly on tilted plates) have been carried out that permit the function C,(Q to be modeled. Observation has also revealed that there are two patterns of turbulent flow detached and attached. Attached flow, where the flow sticks to the body contour, is best exemplified by the flow on a vertical plate, and the C,(Q, = C, (90°) applying in this situation is denoted Cv,. Detached flow, where turbulent eddies rise away from the heated surface, is best exemplified by the flow on a horizontal upward-facing (heated) plate, and the C,(Q = C,(0°) applying in this situation is denoted Cf. The first step in establishing the C,(Q function has been to model how Cf and CJ depend on the Prandtl number the equations for these quantities (justified later) that have been found to best fit currently available data are... [Pg.212]

McNeil Akron Repiquetn, France) single-screw extruder, L/D=25. The composite material was obtained in a granulate form Polish Patent 186577, 2004). The composite granulates were melted in mould between heating plates at the temperature of 200°C under load of 3000 kG to obtain the samples required for the experiments. [Pg.196]

Arcoumanis C, Chang J-C (1993) Heat transfer between a heated plate and an impinging transient diesel spray. Experiments in Fluids 16 105-119. [Pg.453]

Croup A carried out experiments with an electrically heated plate (length L in direction of flow=1 m, area A = 0.5m ) cooled by forced air with a velocity of 10 to 30m s The plate has a very high heat conductivity and thus a uniform temperature. A constant temperature differrence between the plate (with temperature 302 K) and the main stream of air of 2 K is established by adjusting the electrical power. The heating power is then measured as a function of the gas velocity (Figure 3.2.5). [Pg.70]

A variety of studies can be found in the literature for the solution of the convection heat transfer problem in micro-channels. Some of the analytical methods are very powerful, computationally very fast, and provide highly accurate results. Usually, their application is shown only for those channels and thermal boundary conditions for which solutions already exist, such as circular tube and parallel plates for constant heat flux or constant temperature thermal boundary conditions. The majority of experimental investigations are carried out under other thermal boundary conditions (e.g., experiments in rectangular and trapezoidal channels were conducted with heating only the bottom and/or the top of the channel). These experiments should be compared to solutions obtained for a given channel geometry at the same thermal boundary conditions. Results obtained in devices that are built up from a number of parallel micro-channels should account for heat flux and temperature distribution not only due to heat conduction in the streamwise direction but also conduction across the experimental set-up, and new computational models should be elaborated to compare the measurements with theory. [Pg.187]

FIGURE 10.5 Elution profile on OH-B12 treated by microwave heating for 6 min during silica gel 60 column chromatography. Fifty milliliters of the treated OH-B12 solution (5 mmol/1) was evaporated to dryness and dissolved in a small amount of w-butanol/2-pro-panol/water (10 7 10, v/v) as a solvent. The concentrated solution was put on a column (1.4 X 15.0 cm) of silica gel 60 equilibrated with the same solvent and eluted with the same solvent in the dark. The eluate was collected at 4.0 ml with a fraction collector. Fractions I to V were pooled, evaporated to dryness, dissolved with a small amount of distilled water, and analyzed with silica gel TLC. Inset represents the mobile pattern of the OH-B12 degradation products of fractions I to V on the TLC plate. Data are typical, taken from one of five experiments. (Reprinted with permission from Watanabe, F. et al., J. Agric. Food Chem., 46, 5177-5180, 1998. Copyright (1998) American Chemical Society.)... [Pg.244]

HREELS experiments [66] were performed in a UHV chamber. The chamber was pre-evacuated by polyphenylether-oil diffusion pump the base pressure reached 2 x 10 Torr. The HREELS spectrometer consisted of a double-pass electrostatic cylindrical-deflector-type monochromator and the same type of analyzer. The energy resolution of the spectrometer is 4-6 meV (32-48 cm ). A sample was transferred from the ICP growth chamber to the HREELS chamber in the atmosphere. It was clipped by a small tantalum plate, which was suspended by tantalum wires. The sample was radia-tively heated in vacuum by a tungsten filament placed at the rear. The sample temperature was measured by an infrared (A = 2.0 yum) optical pyrometer. All HREELS measurements were taken at room temperature. The electron incident and detection angles were each 72° to the surface normal. The primary electron energy was 15 eV. [Pg.6]


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See also in sourсe #XX -- [ Pg.235 ]

See also in sourсe #XX -- [ Pg.235 ]




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