Big Chemical Encyclopedia

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

Articles Figures Tables About

Channelized fluid

Author Micro-channel Fluid Re Poiseuille number RCcr... [Pg.112]

In this work, the MeOH kinetic model of Lee et al. [9] is adopted for the micro-channel fluid dynamics analysis. Pressure and concentration distributions are investigated and represented to provide the physico-chemical insight on the transport phenomena in the microscale flow chamber. The mass, momentum, and species equations were employed with kinetic equations that describe the chemical reaction characteristics to solve flow-field, methanol conversion rate, and species concentration variations along the micro-reformer channel. [Pg.645]

A channelized fluid leads to local equilibration on the scale of individual beds or units, but does not result in isotopic homogenization of all rocks or units. Channelized flow favors chemical heterogeneity, allowing some rocks to remain unaffected. Although both types of fluid flow appear to be manifest in nature, the latter type appears to be more common. [Pg.220]

A 23-year-old woman took chlorpropamide 5-10 g. She needed assisted respiration and cardiac pacing for bradycardia (probably due to blockade of potassium channels), fluid infusion, and forced diuresis for 3 days. Notwithstanding continuous glucose infusion and glucose boluses she relapsed into severe hypoglycemia with convulsions. Only on day 27 was her urine free of chlorpropamide and her blood glucose normal. [Pg.450]

In the flow of water in open channels, fluid friction is a factor as well as gravity and inertia, and apparently we face the same difficulty here. However, for flow in an open channel there is usually fully developed turbulence, so that the hydraulic friction loss is exactly proportional to V2, as will be shown later. The fluid friction is therefore independent of Reynolds number, with rare exceptions, and thus is a function of the Froude number alone. [Pg.422]

The sedimentation FFF process is illustrated in Figure 1. In this figure, the FFF channel, which has a ribbon-like rather than a tube-like configuration, is curved to fit within a centrifuge basket. The centrifuge is responsible for the sedimentation forces which impel particles toward the accumulation wall. Naturally, the largest and most massive particles are impelled by the greatest forces and end up closest to the wall, provided their density differs from that of the channel fluid. [Pg.216]

Hoisch T. D. (1991) The thermal effects of pervasive and channelized fluid flow in the deep crust. J. Geol. 99, 69-80. [Pg.1488]

The juxtaposition of textural and stable isotope evidence of limited fluid mobility during HP and UHP metamorphism with mineralogical evidence of dehydration and decarbonation, forces one to ask how devolatilization was accomplished. Channelized fluid flow has been found in a number of studies in well-exposed regions such... [Pg.1572]

Figure 5. Gelman pleated crossflow filter cartridge. Cartridge components (A) a porous pleated support screen to provide mechanical support under applied pressure (B) the pleated microporous filtration element (C) the pleated spacer which creates the thin flow channel and promotes turbulent flow (D) the impermeable film which creates the flow channel (E) a porous support tube to provide an exit for permeate (F) open-end cap which provides for exit of product flow (G) closed-end cap completely which seals one end of module (H) outer seal ring which creates the seal between the impermeable film in the module and the interior of the housing. The back pressure support tube is not pictured. The ends of the cartridge are potted and sealed. A space between the ends of Film D and the end seals is provided to allow the entrance and exit of the flow-channel fluid. Figure 5. Gelman pleated crossflow filter cartridge. Cartridge components (A) a porous pleated support screen to provide mechanical support under applied pressure (B) the pleated microporous filtration element (C) the pleated spacer which creates the thin flow channel and promotes turbulent flow (D) the impermeable film which creates the flow channel (E) a porous support tube to provide an exit for permeate (F) open-end cap which provides for exit of product flow (G) closed-end cap completely which seals one end of module (H) outer seal ring which creates the seal between the impermeable film in the module and the interior of the housing. The back pressure support tube is not pictured. The ends of the cartridge are potted and sealed. A space between the ends of Film D and the end seals is provided to allow the entrance and exit of the flow-channel fluid.
Sample, J.C., Reid, M.R., Tobin, H.J. Moore, J.C. (1993) Carbonate cements indicate channeled fluid flow along a zone of vertical faults at the deformation front of the Cascadia accretionary wedge (north-west U.S. coast). Geology, 21, 507-510. [Pg.436]

Conceptually, hollow fibers are the ideal membrane configuration. There is no "parasite drag" and no expensive porous support tube. The fibers may be pressurized on the inside (up to 30 psig) permitting "thin-channel" fluid management of the feed stream (refer to Figure 3.13). [Pg.205]

It is also important to note that these factors influence permeability on different scales as described by Brace (1984), permeabilities measured on the scale of a drill hole (30-300 m) can be much higher, due to widely spaced fractures, than those measured on a laboratory sample (5-15 cm). Thus drill hole permeabilities may be appropriate for estimating the flux of channeled fluids through the crust, but laboratory scale permeability, if properly measured, affords a better estimate of truly pervasive fluid flow. [Pg.455]

Carter, K. E., Dworkin, S. I. 1990. Channelized fluid flow through shear zones during fluid enhanced dynamic recrystallization. Geology, Geological Society of America, 18, 720-723. [Pg.366]

The governing conservation equations developed here lead to a well-posed system of partial differential equations, on specification of the appropriate boundary conditions. It can be noted here that boundary conditions corresponding to DNA hybridization are already incorporated through specification of the source term / , (Eq. 21) for control volumes adjacent to the channel-fluid interface and need not be duplicated in prescription of boundary conditions. Other pertinent boundary conditions are summarized in T able 1. [Pg.855]

The previously described situation where in-channel fluid temperatures encountered are significantly above ambient conditions is... [Pg.3210]

Pettersson et al. [139] fabricated a valve based on polypyrrole bending bilayers attached to rigid polymer plates. They fabricated the actuators on a flat surface, and then bonded that to a polymer cover with the fluid channels. Fluid flow was reduced when the plates were rotated perpendicular to the surface so that they blocked the channel. A similar device has been developed to operate a flap that opens and closes the cover on a microvial for cell clinic processes [140-142]. [Pg.1584]

The single screw RTD is narrower than the flat plate RTD because of the re-circulation of the fluid in the screw channel. Fluid spends more time in the lower portion of the channel = 0 to 2/3 than in the upper portion of the channel = 2/3 to 1. [Pg.487]

S. B. Savage. "Gravity flow of cohesionless granular materials in chutes and channels," /. Fluid Mech., 92, 53-96, 1979. [Pg.97]

Two-dimensional models realistically reproduce the in-channel fluid mechanical transport and, when coupled with detailed hetero-Z homogeneous chemistry, provide a powerful tool for both reactor design and fundamental research. Three-dimensional (3D) reactive flow models are necessary in complex geometries with nonstraight channels and cross-flow between channels used for achieving reactor radial uniformity. ZUthough 3D effects do play a role even for straight-channel honeycomb... [Pg.110]

To overcome the problem Of preserving the mechanical freedom of the element in the channel in a water rig at 1000 Ib/in with a power Input of A MW, the steam and water has to be pre-tnlxed at channel Inlet to simulate the channel outlet conditions required and the element is unheated electrically. Because of the thermal properties of Freon it Is possible to simulate the correct channel fluid conditions with an electrical power input to the fuel element of only about 300 kW, and this can be supplied without any additional constraint to the vibrating system. [Pg.106]

Gaver, D. R, R. W. Samsel et al. 1996. The steady motion of a semi-infinite bubble through a flexible-waUed channel. /. Fluid Mech 319 25-65. [Pg.315]


See other pages where Channelized fluid is mentioned: [Pg.153]    [Pg.158]    [Pg.222]    [Pg.1479]    [Pg.1573]    [Pg.284]    [Pg.158]    [Pg.415]    [Pg.472]    [Pg.57]    [Pg.2651]    [Pg.346]    [Pg.379]    [Pg.379]    [Pg.212]    [Pg.1981]    [Pg.435]    [Pg.194]    [Pg.431]   
See also in sourсe #XX -- [ Pg.220 ]




SEARCH



Channel fluid dynamics

Fluid flow channelized

Fluid parallel flow channels

Isothermal Flow in Channels Newtonian Fluids

Isothermal Flow in Channels Non-Newtonian Fluids

Non-Newtonian Fluids in Tubes and Channels

© 2024 chempedia.info