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Velocity, of spreading

Note some particularities of new USCT method. At first, data collection and search of areas with anomalous (inhomogeneous)SD of acoustic parameters (velocities of spreading of US waves) is joined. As a sought image, on which anomalies is revealed, it is offered total image B (r), which practically is the low frequency copy of restored fimction g(f). As PMF SD of... [Pg.251]

The velocity of spreading on water has been observed by Brinkman,9 Cary and Rideal,10 Ramdas,11 Woog,12 and others. It is often of the order 20 cm. per... [Pg.213]

Thermal diffusivity (m /s) characterizes the velocity of spreading of the temperature in the material and is calculated as... [Pg.35]

The ratio of the velocities of spreading of drops of the same liquid on two bushes made from different pol5oners is... [Pg.454]

Figure 1. The computer plot of the velocity of spreading dA/dt vs time for a drop of clock oil Cuypers 4 on various polymer surfaces. 1 - Tarnoform, 2 - Delrin 500 NC 10, 3 - Tarnamid T-27, 4 -... Figure 1. The computer plot of the velocity of spreading dA/dt vs time for a drop of clock oil Cuypers 4 on various polymer surfaces. 1 - Tarnoform, 2 - Delrin 500 NC 10, 3 - Tarnamid T-27, 4 -...
Figure 2. Coefficient of friction vs. velocity of spreading dX/dt after 2 s of spreading time) for POM, PA 6 and PA 6 + 25% glass fibre materials (from left to right respectively). Figure 2. Coefficient of friction vs. velocity of spreading dX/dt after 2 s of spreading time) for POM, PA 6 and PA 6 + 25% glass fibre materials (from left to right respectively).
There exists a relationship between the tribological properties of the journal polymer miniature bearings and the surface energetics (expressed as the velocity of spreading dX/dt) of the polymer materials and lubricants. [Pg.460]

The friction coefficient and wear of microbearings are high when the velocity of spreading dX/dt, on the bearing polymer surface is high. [Pg.460]

That is, the lower the velocity of spreading, U, the higher the thickness below which the disjoining pressure overcomes the tangential stress. If, as before, we adopt at... [Pg.172]

The time, values relevant for our experiments are calculated below. Let us estimate the Reynolds number during the capillary spreading stage. Equation 4.39 gives the velocity of spreading, which should be used for calculation of the Reynolds number. Simple rearrangement gives... [Pg.328]

FIGURE 4.5 Dimensionless velocity of spreading (v+, solid line) and velocity of drop shrinkage (v, dotted line) on dimensionless time, calculated according to Equation 4.75. Intersection of these two dependences determines the value of the dimensionless time 0.08, when the radius of the drop base reaches its maximum value, = 1 (in dimensionless units). [Pg.342]

Fig. IV-3. Velocity profiles for particles suspended in water with elapsed time, due to spreading of oleic acid. Time after onset of spreading O, 5 sec, , 5 sec. (From Ref. 31.)... Fig. IV-3. Velocity profiles for particles suspended in water with elapsed time, due to spreading of oleic acid. Time after onset of spreading O, 5 sec, , 5 sec. (From Ref. 31.)...
Diffusion Flames in the Transition Region. As the velocity of the fuel jet increases in the laminar to turbulent transition region, an instabihty develops at the top of the flame and spreads down to its base. This is caused by the shear forces at the boundaries of the fuel jet. The flame length in the transition region is usually calculated by means of empirical formulas of the form (eq. 13) where I = length of the flame, m r = radius of the fuel jet, m v = fuel flow velocity, m/s and and are empirical constants. [Pg.519]

In any gas burner some mechanism or device (flame holder or pilot) must be provided to stabilize the flame against the flow of the unbumed mixture. This device should fix the position of the flame at the burner port. Although gas burners vary greatly in form and complexity, the distribution mechanisms in most cases are fundamentally the same. By keeping the linear velocity of a small fraction of the mixture flow equal to or less than the burning velocity, a steady flame is formed. From this pilot flame, the main flame spreads to consume the main gas flow at a much higher velocity. The area of the steady flame is related to the volumetric flow rate of the mixture by equation 18 (81,82)... [Pg.523]

Action potentials, self-propagating. Action potentials of smooth muscle differ from the typical nerve action potential in at least three ways. First, the depolarization phases of nearly all smooth muscle action potentials are due to an increase in calcium rather than sodium conductance. Consequently, the rates of rise of smooth action potentials are slow, and the durations are long relative to most neural action potentials. Second, smooth muscle action potentials arise from membrane that is autonomously active and tonically modulated by autonomic neurotransmitters. Therefore, conduction velocities and action potential shapes are labile. Finally, smooth muscle action potentials spread along bundles of myocytes which are interconnected in three dimensions. Therefore the actual spatial patterns of spreading of the action potential vary. [Pg.193]

Figure 13.7 (a) The self-spreading distance and (b) velocity of egg-PC lipid bilayer in NaCI aqueous solutions with different concentrations, (x) 100mM, (0) 10mM, and ( ) 1 mM. Adapted from Ref [53] with permission. [Pg.231]

The cometary coma The coma and the nucleus form the head of the comet the streams of dust and gas released by the comet form a very large, extremely tenuous atmosphere called the coma, which can have a spread up to around 104—105 km. The coma is not developed when the comet is a long way from the sun, but when it comes closer (at around 5 AU), the ice mixture begins to sublime and is ejected as a gas stream. Dust particles are entrained at a velocity of around one kilometre per second. [Pg.61]

The size, the velocity, and the solid volume fraction of the bubbles and the solids slugs are reflected in the shape and frequency of the force probe response as shown in Fig. 24. The amplitude of the oscillations is a measure of the solid slug velocity and solid volume fraction. Inside the bubbles, the probe response is nearly flat because of the negligible solids fraction inside the bubble. The spread of the peaks and the length of the flat portions of the probe responses are measures of the size and velocity of the solid slugs and gas bubbles respectively. [Pg.279]

Determination of the flame spread parameter, (fc. The following well known expression has been given (( ), (6), etc) for the velocity of the flame front for a slab initially at the temperature T = Tg... [Pg.570]


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