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Channel mixing chamber

The diameter of the copper slabs is about a centimetre smaller than the inner diameter of the stainless steel housing, leaving a channel for the helium flow. The top of housing has a conical shape, to reduce the amount of 3He necessary to have the phase separation in the right position. The total Kapitza resistance at 20 mK is about 45K/W (e.g. a heat leak of 50 xW on the cold plate of the mixing chamber would give a temperature difference of about 2 mK between the liquid and the cold plate). [Pg.356]

Stainless-Steel Mixing Chamber With Machined Channels... [Pg.422]

Figure 1.8 Design of an electrokinetic instability micro mixer, second-generation device, based on the results obtained with the first design given in Figure 1.7. The electrokinetic instability is confined to the square mixing chamber shown in the center of the schematic and, to a small extent, to fluid channel regions attached to it [25] (by courtesy of ACS). Figure 1.8 Design of an electrokinetic instability micro mixer, second-generation device, based on the results obtained with the first design given in Figure 1.7. The electrokinetic instability is confined to the square mixing chamber shown in the center of the schematic and, to a small extent, to fluid channel regions attached to it [25] (by courtesy of ACS).
M 2] [P 2] Injecting a dyed and a colorless stream into the EHD mixer yields a visually homogeneous solution after passage through the mixing chamber channel with the electrodes [94]. [Pg.18]

M 4] [P 3] Using the improved EKI mixer device, bulk-averaged flow velocities in the outlet channel and in the mixing chamber were 0.5 and 0.16 mm s 1, respectively [25]. The corresponding Reynolds number (Re) is 1.5. [Pg.19]

The initial bimodal distribution in the mixing chamber changes to a unimodal distribution after about 2.5 ms of application of the AC field [25, 93], A similar behavior is found for the outlet channel, downstream of the mixing chamber. A slight bimodality is, however, still present, caused by an unmixed stagnant layer in the corner of the mixing chamber. [Pg.20]

The flow in the feed channels is laminar, as is to be expected [41 ]. Owing to the size of the mixing chamber and the high fluid velocities, liquid mixing is expected to have a fast transition from laminar to turbulent Evidence for this is given below. Different from conventional micro mixers, the primary vortices are in the range of about 100 pm, hence smaller than usual. Thus, mixing is different and should be faster. [Pg.109]

Number of mixing units in series 5 Length of V-type mixing chamber and of side channel 900 pm... [Pg.252]

Total depth (for all channels) 100 pm, 150 pm, 200 pm Mixing chamber inlet width, side-arm width 500 pm, 300 pm... [Pg.252]

Arrays with multiple oblique impinging jets are generated via 3-D channel networks which feed fluid from a reservoir via the outlet nozzles of the network into a mixing chamber (see Figures 1.196 and 1.197) [54], Perforated plates contain such arrays. [Pg.264]

These plates are inserted in a T-channel structure in a still thicker plate, directly at the T-junction at the ends of the two feed channels. In this way, a rectangular mixing chamber is formed in the outlet channel of the T-structure, having multinozzle arrays on both sides. The arrays can be positioned with and without offset to collide the jets directly and to let them flow aside. In the latter case, it is thought that eddies are produced at sufficiently high velocity of the jets. [Pg.265]

Mixing chambers are relatively wide and, therefore, the pressure and drag flows are close to each other. A good feel for the mixing condition can be obtained by examining the velocity profiles at various radial positions, as shown in Fig. 9.48. Clearly, the disks drag the fluid toward the channel block, where it must turn around and flow backward in the... [Pg.513]

Fig. 9.49 The evolution of the interfacial area of a viscous Thiokol rubber in a 26.6-cm parallel-disk mixing chamber with a. — 0.5, with the number of turns. The rubber filled up half the chamber with one-quarter cream color (at the channel block at the left side) and one-quarter black. The numbers on the figure indicate the number of turns from 1/4 to 10. [Reprinted by permission from B. David and Z. Tadmor, Laminar Mixing in Co-rotating Disk Processors, Int. Polym. Process., 3, 38-47 (1988).]... Fig. 9.49 The evolution of the interfacial area of a viscous Thiokol rubber in a 26.6-cm parallel-disk mixing chamber with a. — 0.5, with the number of turns. The rubber filled up half the chamber with one-quarter cream color (at the channel block at the left side) and one-quarter black. The numbers on the figure indicate the number of turns from 1/4 to 10. [Reprinted by permission from B. David and Z. Tadmor, Laminar Mixing in Co-rotating Disk Processors, Int. Polym. Process., 3, 38-47 (1988).]...
The dynamic seal is a reverse extruder created by machining small multiple-screw channels onto the rotor end rotating in the closed housing. Because of the helix angle, they will pump melt back into the mixing chamber. [Pg.558]

Continuous, batch, and flow injection modes of hydride generation have been used successfully [39-41]. In the commonly used continuous mode the sample and sodium borohydride solutions are pumped by using a dual-channel peristaltic pump into a mixing chamber. The volatile hydride gas and hydrogen are carried into the plasma with a flowing argon gas and the excess liquid is directed to the drain. [Pg.83]

Fig. 18 Magneto-hydrodynamic disturbance (MHD) micromixer, (a) Cross-section view of an MHD mixer. MHD mixer comprises the following layers (7) channel bottom wall containing the electrodes (2) spacer layers that constitute the mixing chamber (i) cover plates (4) permanent magnet, (b) Deformation of fluid stream resulting from the application of a Lorentz body force (upper panel) and corresponding creation of eddies (lower panel) (Reprinted from [46] with permission. Copyright 2001 Elsevier)... Fig. 18 Magneto-hydrodynamic disturbance (MHD) micromixer, (a) Cross-section view of an MHD mixer. MHD mixer comprises the following layers (7) channel bottom wall containing the electrodes (2) spacer layers that constitute the mixing chamber (i) cover plates (4) permanent magnet, (b) Deformation of fluid stream resulting from the application of a Lorentz body force (upper panel) and corresponding creation of eddies (lower panel) (Reprinted from [46] with permission. Copyright 2001 Elsevier)...
Fig. 5.67 is a view (in direction A-A) of such a mixing chamber which was opened after conveying fine zinc oxide. Opposite the nozzle a deposit in a Venturi-like shape has built up which defines the most effective flow channel at this point. Similar deposits can be found along the line in pneumatic systems that were not optimally designed and/or arranged. [Pg.123]

This type of titration can be implemented (Fig. 7.17) by intercalating into a single-channel FIA system a gradient chamber (partial mixing chamber) or simply a reaction tube (high-speed FIA titrations) [29]. [Pg.220]


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See also in sourсe #XX -- [ Pg.31 , Pg.32 , Pg.34 ]




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