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Tubular 64-channel

A zinc phosphate material formed in the presence of traro-l,2-diaminocyclohexane forms with pores of 24-membered rings and a consequent large amount of free space in the structure, Zn3(P04)2(P03OH)(diaminocyclohexane)-2H20. The tubular channels formed... [Pg.1180]

Ti-SBA-15 mesoporous, titanium-containing silica self-assembly-15 (with uniform, hexagonal, tubular channels) synthesized by using a triblock organic copolymer as a template... [Pg.26]

Morey et al. (25) synthesized Ti-SBA-15 with uniform tubular channels (surface area = 600-900 m2/g, pore volume = 0.6-1.3 cm3/g, average pore diameter = 6.9 nm) by direct and postsynthesis methods by using triblock copolymers, poly(ethylene oxide)-poly(propylene oxide)-poly(ethylene oxide) in... [Pg.169]

CO = rotation speed (rad s-1) Vf = volume flow rate (cm3 s 1 ) rT = radius of wall-tube U = linear velocity of solution (cm s 1 ) 0 = angle between cone surface and rotation axis x = length of tubular/channel electrode w = width of channel electrode d — width of channel h = half-height of channel co = rotation speed of solution (rad s 1) co" = rotation speed of rotating disc (rad s-1). [Pg.385]

The electrochemical impedance may be obtained from potentiostatic or galvanostatic experiments. Alternating current voltammetric techniques are well documented at the DME, as are various kinds of pulse techniques. The former has also been developed at rotating and tubular/channel electrodes. [Pg.427]

F0 appears to contain the proton-conducting channel of the ATP-synthase. If F0 alone is incorporated into lipo-somes, it makes the membranes leaky to protons. The multiple copies of one of the small subunits of F0 may assemble to form a tubular channel across the membrane (see fig. 14.23). [Pg.322]

The porosity associated with the exinitic maceral of the splint coal can be seen more clearly in Figure 4. The large, irregularly shaped pores often form distinct tubular channels, which extend from the apparent center of the spore exine to the boundary between the spore and the surrounding inertinite. Commonly the channels contain spherical particles, who.se identity as the mineral aragonite (CaC03) was based on... [Pg.325]

Y. Wang, J.A. Howell, R.W. Field and D. Wu, Simulation of crossflow filtration for baffled tubular channels and pulsatile flow. /. Membr. Sci., 95 (1994) 243. [Pg.616]

The Norton filters included an original design (tube) filter element and an improved design (lumen) filter element. Overall dimensions of both filter elements were 2.1 cm diameter by 40.2 cm length. The tube element consisted of a bundle of 28 porous tubes and the lumen element consisted of a porous cylinder with 19 tubular channels or lumens extending the length of the cylinder. The filter membrane comprised of the inner surface of the tubes or lumens and had a smaller pore diameter than the non-membrane portions of the filter. Inside diameter of both tubes and lumens was 2.8 mm resulting in a total membrane area 0.091-m2 (1 ft2) for the tube filter and 0.060-m2 (0.65 ft2)for the lumen filter. Membrane pore diameter was 0.45 (1m for both filters. [Pg.357]

Figure 3.5. Dispersion of a sample plug in a straight tubular channel as affected by molecular diffusion with increasing residence time (top) and corresponding RTD curves (bottom). From left to right t = 0.004, t = 0.04, and t = 0.40. For details see text. (According to Ref. 1061, by courtesy of Elsevier Scientific Publishing Co.)... Figure 3.5. Dispersion of a sample plug in a straight tubular channel as affected by molecular diffusion with increasing residence time (top) and corresponding RTD curves (bottom). From left to right t = 0.004, t = 0.04, and t = 0.40. For details see text. (According to Ref. 1061, by courtesy of Elsevier Scientific Publishing Co.)...
Alternatives to tubular channels are transmeinbrane aggregates that enclose a hydrophilic pore. One example is based on poly-p-phenylene oligomers bearing side arms... [Pg.744]

The characteristics of the fluid velocity depend on the design of the hydrodynamic cell and the flow pattern. The latter is said to be laminar when the solution flows smoothly and constantly in parallel layers such that the predominant velocity is that in the direction of the flow. Laminar flow conditions are desirable since accurate descriptions of the solution hydrodynamics are available. On the other hand, under turbulent flow conditions the solution motion is chaotic and the velocities in the directions perpendicular to that of the flow are significant. The transition between the laminar and turbulent regimes is defined in terms of the dimensionless Re5molds number, Re, that is proportional to the relative movement rate between the electrode and solution, and the electrode size, but inversely proportional to the kinematic viscosity of the solution. Thus, for low Re values the flow pattern is laminar and it transits to turbulent as Re increases. For example, in a tubular channel the laminar regime holds for Re < 2300. [Pg.162]

This, in particular, is demonstrated by the pressure loss in liquid flows within cylindrical tubular channels, where Ap is a function of Re in the laminar mode (Re < 2300) and is independent of channel wall roughness [38] ... [Pg.40]

The analysis of turbulent motion physics for a reaction mtjcture in tubular channels of various designs can open the way to a quantitative and scientifically grounded approach for the selection of the optimal geometry, for any fast chemical process, to reduce the diffusion limitation and create uniform conditions for making synthetic products. However, it is necessary to find a solution for another very important problem of theoretical and applied science the temperature mode control of fast chemical processes with high local heat generation in a reaction zone. [Pg.70]

Moreover, the influence of the chemical reaction rate constant and some other physical parameters of the liquid flow (density, viscosity) on the conditions of macroscopic front formation in turbulent flows, allow us to make an assumption about the differences in the nature of the reaction front and mixing front formation. In the first case, the key parameters of the process are the kinetic and diffusion parameters in the second case, however, the key parameters of the process are the convective and turbulent transfer. The influence of density and viscosity, i.e., the parameters which define the hydrodynamic motion mode of the liquid flow in the tubular channels, on the... [Pg.215]


See other pages where Tubular 64-channel is mentioned: [Pg.2008]    [Pg.22]    [Pg.173]    [Pg.149]    [Pg.243]    [Pg.356]    [Pg.403]    [Pg.101]    [Pg.534]    [Pg.197]    [Pg.1766]    [Pg.128]    [Pg.713]    [Pg.577]    [Pg.239]    [Pg.244]    [Pg.245]    [Pg.373]    [Pg.2177]    [Pg.591]    [Pg.61]    [Pg.547]    [Pg.536]    [Pg.2161]    [Pg.358]    [Pg.2012]    [Pg.21]    [Pg.261]    [Pg.25]    [Pg.29]    [Pg.34]    [Pg.44]    [Pg.51]    [Pg.86]   
See also in sourсe #XX -- [ Pg.460 ]




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