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Opening velocity

FIGURE 10.10 Velocity field outside circular (left) and flanged circular (right) opening. Velocities are given on a plane of the diameter and in percentages of opening velocity. [Pg.827]

For enclosures, velocity measurements, in the plane of the opening, offer a quick check on the design conditions. Fiowever, the opening velocity is not a direct measure of the ability of an enclosure to provide personnel protection. Other measures of efficiency are required and depend on use of the enclosure. In the case of safety cabinets and laboratory hoods, allowance factors for protection and leakage are applied to ensure complete safety when in use. [Pg.1014]

Figure 13 shows a quantitative comparison of our results for the early stages for hole growth. Almost all tiny holes (with a diameter D of about 70 nm) were formed after annealing for only 1 min. This implies an average opening velocity AD At) of these holes of about 70 nm/min and an average shear rate AylAt UD ADIAt of about 0.7 min . Comparing AylAt with the reptation time (irep) of PS close to Tg (for the conditions of the experiments shown in Fig. 11, Trep is much larger than one year [104]) demonstrates that on the time scale of the experiments we cannot expect... Figure 13 shows a quantitative comparison of our results for the early stages for hole growth. Almost all tiny holes (with a diameter D of about 70 nm) were formed after annealing for only 1 min. This implies an average opening velocity AD At) of these holes of about 70 nm/min and an average shear rate AylAt UD ADIAt of about 0.7 min . Comparing AylAt with the reptation time (irep) of PS close to Tg (for the conditions of the experiments shown in Fig. 11, Trep is much larger than one year [104]) demonstrates that on the time scale of the experiments we cannot expect...
The decay on the rear side can be fitted to an exponential function y = A exp [(x — Xo)/Ao] + yo with amplitude A and offsets Xq and yo- As expected by theory [42,44,46,47], the characteristic decay length Aq did not vary with annealing time. Fits to the profiles shown in Fig. 16 all resulted in Aq 0.5 pm. We note, however, that Aq could vary between 0.3 pm and several micrometers for samples with slightly varying thicknesses of the PDMS coating. The hole opening velocity was faster for larger Aq. [Pg.47]

Fig. 5. Theory vs. experiment rupture forces computed from rupture simulations at various time scales (various pulling velocities Vcant) ranging from one nanosecond (vcant = 0.015 A/ps) to 40 picoscconds (vcant = 0.375 A/ps) (black circles) compare well with the experimental value (open diamond) when extrapolated linearly (dashed line) to the experimental time scale of milliseconds. Fig. 5. Theory vs. experiment rupture forces computed from rupture simulations at various time scales (various pulling velocities Vcant) ranging from one nanosecond (vcant = 0.015 A/ps) to 40 picoscconds (vcant = 0.375 A/ps) (black circles) compare well with the experimental value (open diamond) when extrapolated linearly (dashed line) to the experimental time scale of milliseconds.
In a skimmed supersonic jet, the parallel nature of the resulting beam opens up the possibility of observing spectra with sub-Doppler resolution in which the line width due to Doppler broadening (see Section 2.3.4) is reduced. This is achieved by observing the specttum in a direction perpendicular to that of the beam. The molecules in the beam have zero velocity in the direction of observation and the Doppler broadening is reduced substantially. Fluorescence excitation spectra can be obtained with sub-Doppler rotational line widths by directing the laser perpendicular to the beam. The Doppler broadening is not removed completely because both the laser beam and the supersonic beam are not quite parallel. [Pg.398]

Fig. 16. Plots showing (a) variation of (c F/2)J. / ) with 1 for O2 (left plot, X, 0.84- 0.72 mm = 20-25 mesh Q 0.42-0.29 mm = 40-50 mesh) and N2 (right plot, on 3.2-mm pellets) in Bergbau-Forschung carbon molecular sieve and (b) variation of HETP with Hquid velocity (interstitial) for fmctose (soHd symbols), and glucose (open symbols) in a column packed with KX 2eoHte crystals. From refs. 22 and 23. Fig. 16. Plots showing (a) variation of (c F/2)J. / ) with 1 for O2 (left plot, X, 0.84- 0.72 mm = 20-25 mesh Q 0.42-0.29 mm = 40-50 mesh) and N2 (right plot, on 3.2-mm pellets) in Bergbau-Forschung carbon molecular sieve and (b) variation of HETP with Hquid velocity (interstitial) for fmctose (soHd symbols), and glucose (open symbols) in a column packed with KX 2eoHte crystals. From refs. 22 and 23.
Pitot Tubes. The fundamental design of a pitot tube is shown in Eigure 9a. The opening into the flow stream measures the total or stagnation pressure of the stream whereas a wall tap senses static pressure. The velocity at the tip opening, lA can be obtained by the Bernoulli equation ... [Pg.61]

Gup and Vane Anemometers. A number of flow meter designs use a rotating element kept in motion by the kinetic energy of the flowing stream such that the speed is a measure of fluid velocity. In general, these meters, if used to measure wind velocity, are called anemometers if used for open-channel Hquids, current meters and if used for closed pipes, turbine flow meters. [Pg.63]

Laser Doppler Velocimeters. Laser Doppler flow meters have been developed to measure Hquid or gas velocities in both open and closed conduits. Velocity is measured by detecting the frequency shift in the light scattered by natural or added contaminant particles in the flow. Operation is conceptually analogous to the Doppler ultrasonic meters. Laser Doppler meters can be appHed to very low flows and have the advantage of sensing at a distance, without mechanical contact or interaction. The technique has greatest appHcation in open-flow studies such as the deterrnination of engine exhaust velocities and ship wake characteristics. [Pg.67]

The special design of the Latham bowl allows for a specific blood cell separation known as SURGE. This technique makes use of the principle of critical velocity. The Latham bowl is filled until the huffy coat, ie, layer of platelets and white cells, moves in front of the bowl optics. At this point the machine starts to recirculate plasma through the bowl at increasing rates. The smallest particles, ie, platelets, ate the first to leave the bowl. Their high number causes the effluent line to turn foggy. The optical density of the fluid in the effluent line is monitored by the line sensor. A special algorithm then determines when to open and close the appropriate valves, as well as the optimum recirculation rate. [Pg.523]

Although it has been common practice to specify the pressure loss in ordinary valves in terms of either equivalent length of straight pipe of the same size or velocity head loss, it is becoming more common to specify flow rate and pressure drop characteristics in the same terms as has been the practice for valves designed specifically for control service, namely, in terms of the valve coefficient, C. The flow coefficient of a valve is defined as the volume of Hquid at a specified density that flows through the fully opened valve with a unit pressure drop, eg, = 1 when 3.79 L/min (1 gal /min) pass through the valve... [Pg.57]


See other pages where Opening velocity is mentioned: [Pg.830]    [Pg.845]    [Pg.846]    [Pg.876]    [Pg.975]    [Pg.1019]    [Pg.371]    [Pg.128]    [Pg.600]    [Pg.12]    [Pg.830]    [Pg.845]    [Pg.846]    [Pg.876]    [Pg.975]    [Pg.1019]    [Pg.371]    [Pg.128]    [Pg.600]    [Pg.12]    [Pg.1424]    [Pg.113]    [Pg.615]    [Pg.34]    [Pg.116]    [Pg.408]    [Pg.91]    [Pg.104]    [Pg.105]    [Pg.105]    [Pg.61]    [Pg.83]    [Pg.95]    [Pg.310]    [Pg.17]    [Pg.97]    [Pg.232]    [Pg.265]    [Pg.373]    [Pg.291]    [Pg.426]    [Pg.302]    [Pg.398]    [Pg.404]    [Pg.435]    [Pg.464]    [Pg.461]    [Pg.476]   
See also in sourсe #XX -- [ Pg.1019 ]




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