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Drops velocities

Piezoelecttic impulse ink-jet printers ate especially sensitive to bubbles in the ink. A bubble in the firing chamber absorbs some of the comptessional force from the flexing of the chamber wall and reduces drop volume and drop velocity, thereby affecting print quaHty. Because of the limited range of motion of the crystal, bubbles ate not readily ejected, and the loss of print quaHty owing to their presence is persistent. [Pg.53]

Maynes and Webb (2002) presented pressure drop, velocity and rms profile data for water flowing in a tube 0.705 mm in diameter, in the range of Re = 500-5,000. The velocity distribution in the cross-section of the tube was obtained using the molecular tagging velocimetry technique. The profiles for Re = 550,700,1,240, and 1,600 showed excellent agreement with laminar flow theory, as presented in Fig. 3.2. The profiles showed transitional behavior at Re > 2,100. In the range Re = 550-2,100 the Poiseuille number was Po = 64. [Pg.110]

Stepped-diameter pipelines to minimize pressure drop, velocity, wear and power consumption. [Pg.714]

Many attempts have been made to obtain general expressions for pressure drop and mean velocity for flow through packings in terms of voidage and specific surface, as these quantities are often known or can be measured. Alternatively, measurements of the pressure drop, velocity, and voidage provide a convenient way of measuring the surface area of some particulate materials, as described later. [Pg.194]

The measured relation between individual drop velocity Vp, and drop diameter dp is well represented by the following equation [2] ... [Pg.390]

Now the two-phase flow in a nonpulsed eountercurrent column will be discussed. If the continuous liquid flows toward the drops, the drop velocity decreases, whereas the holdup of the drops in the flow system increases if... [Pg.391]

Fig. 9.12 Stationary relative velocity v, of the drop swarms related to the single drop velocity Vp is dependent on the drop hold-up, and Archimedes number Ar. (From Ref. 2.)... [Pg.393]

The Richardson-Zaki equation has been found to agree with experimental data over a wide range of condifions. Equally, if is possible fo use a pressure drop-velocity relationship such as Ergun to determine minimum fluidization velocity, just as for gas-solid fluidizafion. An alternative expression, which has the merit of simplicify, is fhaf of Riba ef al. (1978)... [Pg.50]

Any consideration of mass transfer to or from drops must eventually refer to conditions in the layers (usually thin) of each phase adjacent to the interface. These boundary layers are envisioned as extending away from the interface to a location such that the velocity gradient normal to the general flow direction is substantially zero. In the model shown in Fig. 8, the continuous-phase equatorial boundary layer extends to infinity, but the drop-phase layer stops at the stagnation ring. At drop velocities well above the creeping flow region there is a thin laminar sublayer adjacent to the interface and a thicker turbulent boundary layer between this and the main body of the continuous phase. [Pg.78]

Two other observations are of interest P does not depend on hammer drop height (or drop velocity)... [Pg.314]

A two-part series, Designing Oil and Gas Production Systems" by Arnold and Stewart, provides theory and background requirements for selecting two- and three-phase separators. Formulas for liquid-drop velocity, drop diameter, and liquid retention time, as well as step-by-step procedures for selecting both types of separators, are included. Tables provide a means of simplifying vessel sizing calculations. [Pg.76]

Oll/water settling. Flow around settling oil drops in water or water drops in oil is laminar, so Stokes Law governs. Terminal drop velocity is ... [Pg.100]

On the other hand, the photographic methods have two definite disadvantages. Droplets smaller than 20 microns cannot be photographed satisfactorily in a fast-moving spray, and the photograph records the spatial rather than the more important temporal distribution of drops. The latter objection can be overcome if drop velocities are known, but data on velocities are not easily obtained. Another serious problem is determination of whether a droplet is in or out of focus when it appears near the boundary of the field... [Pg.159]

The SADARM system is thought to be unique because it uses a passive mm wave radiometric sensor in a high spin mode at low altitude — for the first time ever in a munition it uses a vortex ring parachute that maintains a constant spin rate and drop velocity, and is exceptionally stable and it delivers a long-standoff fragment warhead with armor-penetrating capability Ref Anon, ARRADCOM Voice (Oct 17,1977), 7... [Pg.233]

The principal outputs are deposition and drift, but the models can be programmed to give intermediate information on drop velocity, evaporation, flow fields, and other factors. [Pg.85]

Figure 15. Vertical drop velocity from wake effects. Figure 15. Vertical drop velocity from wake effects.
Extraction can be enhanced by the application of a dc or pulsed electric field, typically on the order of 1 kV/cm. This requires that the aqueous phase be dispersed and the organic phase be of low conductivity. The improvement in mass transfer rate is due to the breakup of large drops by the action of the field and to the increase of drop velocity resulting in increased mass transfer coefficients. It has also been found that low-frequency pulsed fields are effective in breaking up emulsions in the settler stage of mixer-settler units. [Pg.503]

Fthenakis, Schatz, and Zakkay 1991 Develop computer simulationss of the Hawk, Nevada Test Site, field tests of water sprays to absorb HF releases. Computer model HFSPRAY developed amd validated against all the Hawk field data. Accurate specification of nozzle parameters is essential sensitivity analysis with model indicated that not only drop size variations but also variation of initial drop velocity and spray pattern can have a measurable effect on model predictions. [Pg.61]

Drop placement accuracy Exact drop landing position is uncertain, due to various parameters such as jet-to-jet variations, single jet-overtime, sensitivity to nozzle straightness, nozzle and surface wetting, nozzle plate contamination, ink formulation and condition, and drop velocity. This issue is worse for longer flight paths or "throw distance". [Pg.17]

Fig. 3. The effect of resistor fouling problems (kogation and decel) on drop velocity. Fig. 3. The effect of resistor fouling problems (kogation and decel) on drop velocity.
In Inkjet technology used by PolyJet for material deposition, the material hquid physical properties are of utmost importance. One of these properties is the material viscosity, which is of primary importance during droplet formation. The viscosity also influences drop velocity the higher the viscosity, the slower the drop velocity and the smaller its volume. [Pg.264]

Based on end of extraction column. No continuous phase resistance. ki d.osc in cm/s, = drop velocity relative to continuous phase. [Pg.440]


See other pages where Drops velocities is mentioned: [Pg.680]    [Pg.680]    [Pg.1477]    [Pg.1477]    [Pg.1480]    [Pg.265]    [Pg.377]    [Pg.395]    [Pg.65]    [Pg.65]    [Pg.146]    [Pg.233]    [Pg.55]    [Pg.56]    [Pg.340]    [Pg.65]    [Pg.69]    [Pg.267]    [Pg.265]    [Pg.72]    [Pg.6]    [Pg.126]    [Pg.128]    [Pg.129]    [Pg.145]    [Pg.505]    [Pg.505]    [Pg.1300]    [Pg.1300]   
See also in sourсe #XX -- [ Pg.59 , Pg.60 , Pg.61 , Pg.62 , Pg.63 , Pg.64 , Pg.65 , Pg.66 ]




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