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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]

Approach to restoring of stresses SD in the three-dimensional event requires for each pixel determinations of matrix with six independent elements. Type of matrixes depends on chosen coordinate systems. It is arised a question, how to present such result for operator that he shall be able to value stresses and their SD. One of the possible ways is a calculation and a presenting in the form of image of SD of stresses tensor invariants. For three-dimensional SDS relative increase of time of spreading of US waves, polarized in directions of main axises of stresses tensor ... [Pg.252]

Before proceeding to the main subject of this chapter—namely, the behavior and properties of spread films on liquid substrates—it is of interest to consider the somewhat wider topic of the spreading of a substance on a liquid surface. Certain general statements can be made as to whether spreading will occur, and the phenomenon itself is of some interest. [Pg.104]

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.)...
The topic of spreading rates is of importance in the technology of the use of mono-layers for evaporation control (see Section IV-6) it is also important, in the opposite sense, in the lubrication of fine bearings, as in watches, where it is necessary that the small drop of oil remain in place and not be dissipated by spreading. Zisman and coworkers have found that spreading rates can be enhanced or reduced by the presence of small amounts of impurities in particular, strongly adsorbed surfactants can form a film over which the oil will not spread [48]. [Pg.111]

Buhaenko M R, Goodwin J W, Riohardson R M and Daniel M F 1985 The influenoe of shear visoosity of spread monolayers on the Langmuir-Blodgett prooess Thin Solid Films 134 217-26... [Pg.2630]

Variance Another common measure of spread is the square of the standard deviation, or the variance. The standard deviation, rather than the variance, is usually reported because the units for standard deviation are the same as that for the mean value. [Pg.57]

Realizing that our data for the mass of a penny can be characterized by a measure of central tendency and a measure of spread suggests two questions. Eirst, does our measure of central tendency agree with the true, or expected value Second, why are our data scattered around the central value Errors associated with central tendency reflect the accuracy of the analysis, but the precision of the analysis is determined by those errors associated with the spread. [Pg.57]

Evaluating Indeterminate Error Although it is impossible to eliminate indeterminate error, its effect can be minimized if the sources and relative magnitudes of the indeterminate error are known. Indeterminate errors may be estimated by an appropriate measure of spread. Typically, a standard deviation is used, although in some cases estimated values are used. The contribution from analytical instruments and equipment are easily measured or estimated. Indeterminate errors introduced by the analyst, such as inconsistencies in the treatment of individual samples, are more difficult to estimate. [Pg.63]

Consider, for example, the data in Table 4.1 for the mass of a penny. Reporting only the mean is insufficient because it fails to indicate the uncertainty in measuring a penny s mass. Including the standard deviation, or other measure of spread, provides the necessary information about the uncertainty in measuring mass. Nevertheless, the central tendency and spread together do not provide a definitive statement about a penny s true mass. If you are not convinced that this is true, ask yourself how obtaining the mass of an additional penny will change the mean and standard deviation. [Pg.70]

For proper use of the equations, the chamber shape must conform to the spray pattern. With cocurrent gas-spray flow, the angle of spread of single-fluid pressure nozzles and two-fluid pneumatic nozzles is such that wall impingement wiU occur at a distance approximately four chamber diameters below the nozzle therefore, chambers employing these atomizers should have vertical height-to-diameter ratios of at least 4 and, more usually, 5. The discharge cone below the vertical portion should have a slope of at least 60°, to minimize settling accumulations, and is used entirely to accelerate gas and solids for entty into the exit duct. [Pg.1238]

Restrietion of spread by means of baffles, ehokes or by advanee inerting. [Pg.191]

Fig. 12. The morphology of spreading. Liquid advances over the solid by means of a precursor foot (usually a few to a few hundred nanometers in thickness) moving out typically several millmeters ahead of the nominal bulk liquid interline. Fig. 12. The morphology of spreading. Liquid advances over the solid by means of a precursor foot (usually a few to a few hundred nanometers in thickness) moving out typically several millmeters ahead of the nominal bulk liquid interline.
Contact angle, 0, and spreading coefficient for a liquid on a solid surface comparison of spreading coefficient S for a smooth surface with S for a surface of roughness factor r... [Pg.321]

Methods of estimating gaseous effluent concentrations have undergone many revisions. For a number of years, estimates of concentrations were calculated from the equations of Sutton, with the atmospheric dispersion parameters C, C, and n, or from the equations of Bosanquet with the dispersion parameters p and Q. More common approaches are based on experimental observation that the vertical distribution of spreading particles from an elevated point is... [Pg.284]

Fig. 4.5-6 Example of Spread in HEPsfrom IPE for BWKs "Failure to Depressurize ... Fig. 4.5-6 Example of Spread in HEPsfrom IPE for BWKs "Failure to Depressurize ...
A fire in a bulk storage facility at Coode Island, Melbourne, Australia, in August 1991 caused extensive damage and many complaints about the pollution caused by the smoke plume, but no injuries. The tank vents were connected together and piped to a carbon bed vapor recovery system. There were no flame arrestors in the pipework. Whatever the cause of the initial fire or explosion, the vent collection system provided a means of spreading the fire from one tank to another. [Pg.72]

From Table 12.2.1, assume the oil layer height h in a rough sea to be 0.05 inch. If the oil is distributed radially from tlie point of discharge in the form of a cylinder 0.05 inch high, tlie radius of spread is given by... [Pg.386]

Tlie expected value of a random variable X is also called "the mean of X" and is often designated by p. Tlie expected value of (X-p) is called die variance of X. The positive square root of the variance is called die standard deviation. Tlie terms and a (sigma squared and sigma) represent variance and standard deviadon, respectively. Variance is a measure of the spread or dispersion of die values of the random variable about its mean value. Tlie standard deviation is also a measure of spread or dispersion. The standard deviation is expressed in die same miits as X, wliile die variance is expressed in the square of these units. [Pg.559]

In tlie case of a random sample of observations on a continuous random variable assumed to have a so-called nonnal pdf, tlie graph of which is a bellshaped curve, tlie following statements give a more precise interpretation of the sample standard deviation S as a measure of spread or dispersion. [Pg.563]


See other pages where Of spreading is mentioned: [Pg.381]    [Pg.248]    [Pg.248]    [Pg.250]    [Pg.252]    [Pg.3]    [Pg.110]    [Pg.111]    [Pg.113]    [Pg.147]    [Pg.466]    [Pg.542]    [Pg.552]    [Pg.55]    [Pg.56]    [Pg.435]    [Pg.235]    [Pg.235]    [Pg.291]    [Pg.1830]    [Pg.51]    [Pg.197]    [Pg.25]    [Pg.26]    [Pg.78]    [Pg.531]    [Pg.469]    [Pg.412]   
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Capillary Forces during Initial Stage of Spreading

Dry spreading of liquids on solids

Dynamics of Spreading

Examples of Other Flame Spread Conditions

Experimental determination of spreading pressure in monolayers Langmuir balance

Flame Spread Indexes and Fire Rating of Composite Materials

Free energy of spreading

Gravitational Regime of Spreading

Insoluble Monolayers Spreading of Surfactants on Aqueous

Interaction, Spreading and Splashing of Multiple Droplets on a Surface

Kinetics of Spreading Processes

Kinetics of spreading

Lateral spreading of dopants

Linear spreading of perturbations

Measurement of spread

Molecular Basis of Zone Spreading

Next page spread of, factory farms and

Non-Spreading (Partial Wetting) by Hydrocarbons on the Surfaces of Aqueous Surfactant Solutions

Principles of fire spread

Principles of heat transmission and fire spread

Processes of flame spread

Quasi-Steady-State Approach to the Kinetics of Spreading

Regime of Spreading

Robust estimates of location and spread

Role of Surfactants in Wetting, Spreading and Adhesion

Role of antifoam spreading

Smooth Particles with Edges in Absence of Spread Oil Layers

Smooth Particles with Edges in Presence of Spread Oil Layers

Spherical Particles, Spread Oil Layers, and Rupture of Pseudoemulsion Films

Spread Monolayers of Protein

Spread of Infection

Spread of cell injury

Spread of detonation

Spread of distributions

Spread of fires

Spread of flames

Spread of results

Spread, of data

Spreading Awareness of Traffic Safety through Web Application

Spreading Behavior of Oils

Spreading Behavior of Typical Antifoam Oils on Aqueous Surfaces

Spreading of Aqueous Surfactant Solutions over Porous Layers

Spreading of Liquid Drops over Dry Porous Layers Complete Wetting Case

Spreading of Liquid Drops over Saturated Porous Layers

Spreading of Liquid Drops over Thick Porous Substrates Complete Wetting Case

Spreading of Non-Newtonian Liquids over Solid Substrates

Spreading of Polymer Solution

Spreading of Substances

Spreading of Surfactant Solutions over Hydrophobic Substrates

Spreading of Very Thin Droplets

Spreading of cold dense clouds

Spreading of droplets

Spreading of liquids

Spreading of liquids on solids

Spreading of liquids on surfaces

Spreading of one liquid on another

Spreading of size

Spreading of surfactant

Spreading of the chromatographic zone

Spreading of the liquid

States of Lipid Monolayers Spread on Water Surface

States of Monolayers Spread on Water Surface

Surface spread of flame test

Technology of Spread Manufacture

Term structure of credit spreads

The Spread of Williamsonian Theory

The Spreading of One Liquid on Another

The dynamics of dry spreading

The formation of surface films by spontaneous spreading from solids

The mechanism of spreading on liquids

Thermodynamics of Wetting and Spreading

Thick films - spreading of one liquid on another

Two Types of Wetting The Spreading Parameter

Velocity, of spreading

Wetting or Spreading in the Presence of Surfactants

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