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Flow-through channel

Perforated Plates and Screens A nonuniform velocity profile in turbulent flow through channels or process equipment can be smoothed out to any desired degree by adding sufficient uniform resistance, such as perforated plates or screens across the flow channel, as shown in Fig. 6-38. Stoker Ind. Eng. Chem., 38, 622-624 [1946]) provides the following equation for the effect of a uniform resistance on velocity profile ... [Pg.659]

In many channels the relation between current and membrane potential is nonlinear. These channels show rectification, i.e., the property of the channel to conduct ions more readily in one direction than in the other. Depending on the preferential current flow through channels, these are described as outward or inward rectifying. [Pg.1063]

According to Eq. (14) the maximum velocity gradient at the wall is at y = D/2. It amounts to (du/dy) ju=C u/D. The stress derived from this with Eq. (1) has been used in a number of studies (see e.g. [8-11]) as a measure of stress. However, particles are only subjected to this maximum stress if they close to y = 0. As this cannot or can only temporarily be the case during flow through channels, such test results should be regarded with caution and only conditionally suitable for comparison with the results from other model apparatuses, not to mention bioreactors. [Pg.48]

However, in contrast to the two classes of dispersive mixers mentioned before, the attached flow-through channel contains a packed bed of particles which may carry a catalyst. This chamber is much larger than the typical dimensions of the inlet channels (e.g. compare with Section 5.1.2). The packed bed and its interstices influence the gas/liquid flow patterns, e.g. a trickle-bed operation may be established. [Pg.593]

The major design concept of polymer monoliths for separation media is the realization of the hierarchical porous structure of mesopores (2-50 nm in diameter) and macropores (larger than 50 nm in diameter). The mesopores provide retentive sites and macropores flow-through channels for effective mobile-phase transport and solute transfer between the mobile phase and the stationary phase. Preparation methods of such monolithic polymers with bimodal pore sizes were disclosed in a US patent (Frechet and Svec, 1994). The two modes of pore-size distribution were characterized with the smaller sized pores ranging less than 200 nm and the larger sized pores greater than 600 nm. In the case of silica monoliths, the concept of hierarchy of pore structures is more clearly realized in the preparation by sol-gel processes followed by mesopore formation (Minakuchi et al., 1996). [Pg.148]

Fig. 10.17 Specific detection of HSV 1. Phase changes A Fig. 10.17 Specific detection of HSV 1. Phase changes A<P14 and A 24 in the four channel YI sensor as a function of time during several processes. HSA solution was first flowed through channels 1 and 2 simultaneously (Al and A2). Next, after washing with PBS, HSV 1 solution was flowed in channels 1 and 2 simultaneously (B1 and B2) PBS was continuously flowed in reference channel 4. Thus, the four graphs show the following interactions (Al) a HSA HSA, (A2) a HSV 1 gG HSA, (Bl) a HSA HSV 1, (B2) a HSV 1 gG HSV 1. Note that initial phases in Al and A2 were shifted to 0 for clarity. Reprinted from Ref. 28 with permission. 2008 American Chemical Society...
FIGURE 13.7 Scanning electron micrograph showing flow-through channels in silica-based monolithic rods. [Pg.347]

The brain lacks connection with the lymphatic system. The interstitial fluid drains into the perivascular space, which surrounds arteries and veins, and from there into the sub-arachnoid space where it mixes with the cerebrospinal fluid. This is secreted by the choroid plexuses, which are capillary-rich outgrowths into cavities within the brain, known as ventricles. From the ventricles, cerebrospinal fluid flows through channels to the surface of the brain and... [Pg.310]

El. Eckert, E. R. G., Diaguila, A. J., and Donoughe, P. L., Experiments on turbulent flow through channels having porous rough surfaces with or without air injection. NACA Tech. Note 3339 (1955). [Pg.231]

Mini-Packed-Bed Reactors Packed-bed microreactors have a larger flow-through channel that contains particles brought into contact [274,277,278]. The flow of the gas-liquid mixture goes through the interstices, and in this way a dispersive action is given, that is, continuously renewing the interfaces. [Pg.153]

Another design for the electrochemical formation of radicals directly in the cavity involved the flow-through channel cell shown in Fig. 56 [370]. The cell was constructed in synthetic silica to avoid interference with the microwave field. The flow through this cell was demonstrated to be laminar up to Reynolds numbers less than 10, which allowed for the derivation of quantitative relations between the ESR signal, the flow rate, and the current. [Pg.168]

Figure 56. View of a flow-through channel cell (unassembled), showing cover place with electrode and lead-out wire, channel plate, and one of two PTFE mounting spacers. (From Ref. 370.)... Figure 56. View of a flow-through channel cell (unassembled), showing cover place with electrode and lead-out wire, channel plate, and one of two PTFE mounting spacers. (From Ref. 370.)...
Some empirical equations for heat and mass transfer in flow through channels, packed and fluidised beds... [Pg.370]

Fig. 10 illustrates upward vertical flow through channels. It is possible of course that vertical downward flow may be encountered. It would be anticipated that the regimes would be modified under these conditions. [Pg.983]

The prediction of groundwater flow is complicated by the heterogeneities of the subsurface environment, which occur on multiple scales. To understand the evolution of groundwater composition, it is also important to distinguish between flow through porous media and flow through channels (caused by dissolution of the rock matrix) or fractures (resulting from tectonic activity). Such differences in texture can result in differences in the contact between the fluid and mineral surfaces. [Pg.133]

FRICTION FACTOR IN FLOW THROUGH CHANNELS OF NONQRCULAR CROSS SECTION. The friction in long straight channels of constant noncircular cross section can be estimated by using the equations for circular pipes if the diameter in the Reynolds number and in the definition of the friction factor is taken as an equivalent diameter, defined as four times the hydraulic radius. The hydraulic radius is denoted by r and in turn is defined as the ratio of the cross-sectional area of the channel to the wetted perimeter of the channel ... [Pg.103]

This method relies on the simple principle that the flow of ions into an electrolyte-filled micropipette as it nears a surface is dependent on the distance between the sample and the mouth of the pipette [211] (figure Bl.19.40). The probe height can then be used to maintain a constant current flow (of ions) into the micropipette, and the technique functions as a non-contact imaging method. Alternatively, the height can be held constant and the measured ion current used to generate the image. This latter approach has, for example, been used to probe ion flows through channels in membranes. The lateral resolution obtainable by this method depends on the diameter of the micropipette. Values of 200 nm have been reported. [Pg.1718]

Figure 3. Scheme of a flow-through channel electrolyser with plate electrodes d distance between electrodes, L electrode height, w electrode width, v linear velocity of electrolyte. [Pg.54]


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Flow channels

Flow-through

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