Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Gradient thickness

Fig. 2 Flow coaler for creating polymer gradient thickness libraries A doctor blade B polymer solution C substrate D thickness library E x-translation stage F y-translation stage (for characterization). Fig. 2 Flow coaler for creating polymer gradient thickness libraries A doctor blade B polymer solution C substrate D thickness library E x-translation stage F y-translation stage (for characterization).
Finally, that work was summarized by Thostenson and Chou, who showed that both numerical and experimental results indicated that volumetric heating due to microwaves promoted an inside-out cure of the thick laminates and dramatically reduced the overall processing time [115]. Under conventional thermal conditions, to reduce thermal gradients, thick laminates were processed at lower cure temperature and heated with slow heating rates, resulting in excessive cure times. Outside-in curing of the autoclave processed composite resulted in visible matrix cracks, while cracks could not be seen in the microwave-processed composite. The formation of cure gradients within the two composites cured under both micro-wave and conventional conditions are presented in Fig. 31. [Pg.243]

When Ca " " was omitted 0.2 mM EGTA was added. Thereafter at different time intervals the retinas were removed from the incubation media and homogenized with chloroform-methanol by means of a Potter-Elvehjem homogenizer (Folch et al., 1957). Phospholipid classes were isolated by two-dimensional TLC (Rouser et al., 1970) and neutral glycerides by gradient-thickness TLC (Bazan Bazan, 1975). [Pg.482]

Thermal thickness fluctuations in pseudoemulsion films mean that the amounts of adsorbed oil will vary with film thickness as a consequence of different rates of transport of oil molecules arising from differences in concentration gradient. Thinner parts of the film will therefore experience a transient lowering of air-water surface tension relative to adjacent thicker parts of the film. The resultant surface tension gradient will drive liquid away from the thinner parts of the film to the thicker parts of the film, which will increase the concentration gradient. Thickness fluctuations will therefore be amplified and will tend to destabilize the film. Amplification of such thickness fluctuations is opposed by both disjoining pressures, if dfl woCWd < 0, and capillarity. [Pg.78]

Minimum exposure times must be observed in order to reach the requisite S/N ratio. As per EN 1435 and EN 584-1, for the different ranges of utilization (energy, wall thickness), definite film elasses are prescribed. They are characterized by the minimum gradient-to-noise ratios. Based on this, one can calculate the minimum values for the S/N ratio based on the IP systems. The exposure time and the device parameter sensitivity and dynamics (latitude) must be adjusted accordingly, with an availability of an at least 12 bit system for the digitalization. [Pg.474]

O, a large current is detected, which decays steadily with time. The change in potential from will initiate the very rapid reduction of all the oxidized species at the electrode surface and consequently of all the electroactive species diffrising to the surface. It is effectively an instruction to the electrode to instantaneously change the concentration of O at its surface from the bulk value to zero. The chemical change will lead to concentration gradients, which will decrease with time, ultimately to zero, as the diffrision-layer thickness increases. At time t = 0, on the other hand, dc-Jdx) r. will tend to infinity. The linearity of a plot of i versus r... [Pg.1929]

Figure 9.5a shows a portion of a cylindrical capillary of radius R and length 1. We measure the general distance from the center axis of the liquid in the capillary in terms of the variable r and consider specifically the cylindrical shell of thickness dr designated by the broken line in Fig. 9.5a. In general, gravitational, pressure, and viscous forces act on such a volume element, with the viscous forces depending on the velocity gradient in the liquid. Our first task, then, is to examine how the velocity of flow in a cylindrical shell such as this varies with the radius of the shell. Figure 9.5a shows a portion of a cylindrical capillary of radius R and length 1. We measure the general distance from the center axis of the liquid in the capillary in terms of the variable r and consider specifically the cylindrical shell of thickness dr designated by the broken line in Fig. 9.5a. In general, gravitational, pressure, and viscous forces act on such a volume element, with the viscous forces depending on the velocity gradient in the liquid. Our first task, then, is to examine how the velocity of flow in a cylindrical shell such as this varies with the radius of the shell.
Thermal Stresses. When the wak of a cylindrical pressure vessel is subjected to a temperature gradient, every part expands in accordance with the thermal coefficient of linear expansion of the steel. Those parts of the cylinder at a lower temperature resist the expansion of those parts at a higher temperature, so setting up thermal stresses. To estimate the transient thermal stresses which arise during start-up or shutdown of continuous processes or as a result of process intermptions, it is necessary to know the temperature across the wak thickness as a function of radius and time. Techniques for evaluating transient thermal stresses are available (59) but here only steady-state thermal stresses are considered. The steady-state thermal stresses in the radial, tangential, and axial directions at a point sufficiently far away from the ends of the cylinder for there to be no end effects are as fokows ... [Pg.85]

Seldom is the temperature difference across the wall thickness of an item of equipment known. Siace large temperature gradients may occur ia the boundary layers adjacent to the metal surfaces, the temperature difference across the wall should not be estimated from the temperatures of the fluids on each side of the wall, but from the heat flux usiag equation 27... [Pg.86]


See other pages where Gradient thickness is mentioned: [Pg.385]    [Pg.580]    [Pg.449]    [Pg.13]    [Pg.178]    [Pg.481]    [Pg.378]    [Pg.490]    [Pg.1012]    [Pg.229]    [Pg.385]    [Pg.580]    [Pg.449]    [Pg.13]    [Pg.178]    [Pg.481]    [Pg.378]    [Pg.490]    [Pg.1012]    [Pg.229]    [Pg.117]    [Pg.180]    [Pg.214]    [Pg.233]    [Pg.286]    [Pg.526]    [Pg.176]    [Pg.468]    [Pg.1529]    [Pg.1543]    [Pg.2374]    [Pg.588]    [Pg.622]    [Pg.634]    [Pg.393]    [Pg.2]    [Pg.3]    [Pg.63]    [Pg.381]    [Pg.429]    [Pg.297]    [Pg.85]    [Pg.85]    [Pg.173]    [Pg.204]    [Pg.524]    [Pg.236]    [Pg.418]    [Pg.198]    [Pg.155]    [Pg.253]   
See also in sourсe #XX -- [ Pg.10 , Pg.11 , Pg.72 , Pg.73 , Pg.325 ]




SEARCH



© 2024 chempedia.info