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Gravity controller

For NRc S 10, the liquid motion moves with the impeller, and off from the impeller, the fluid is stagnant [34]. The Froude number accounts for the force of gravity when it has a part in determining the motion of the fluid. The Froude numbers must be equal in scale-up situations for the new design to have similar flow when gravity controls the motion [16]. [Pg.300]

Comparison of the boundaries of the observed flow patterns with the analytical criteria derived by Quandt showed that the bubble, dispersed, and annular flow patterns are subclasses of a pressure gradient-controlled flow. Similarly, flow patterns identified as slug, wave, stratified, and f ailing film are subclasses of a gravity-controlled situation. [Pg.159]

This paper reports a summary of lignification values and phenylalanine ammonia lyase (PAL) and peroxidase activity from the STS-3 and STS-51F experiments. The results show a reduction in both lignification and enzyme activity in flight seedlings as compared to one gravity control seedlings. [Pg.204]

In compact geometries the heat transfer coefficient depends on the two-phase flow pattern (51-67). For low condensation rates, the heat transfer is gravity controlled, and the heat transfer coefficient depends on the liquid film thickness. For higher condensation rates, the heat transfer coefficient depends on the vapor shear effect, and for small passages the liquid-vapor interaction leads to high heat transfer coefficients. [Pg.157]

Vapor Shear Controlling For vertical in-tube condensation with vapor and liquid flowing concurrently downward, if gravity controls, Figs. 5-7 and 5-8 may be used, if vapor shear controls, the Carpenter-Colburn correlation (General Discussion on Heat Transfer, London, 1951, ASME, New York, p. 20) is applicable ... [Pg.14]

Columns whose flow of ion exchanger is gravity controlled have been described in the literature [62-67]. The scheme for such column operation is presented in Fig. 25 where the combination of a screw for the removal of ion exchanger from the column at the desired speed and a system consisting of two tanks for the output of ion exchanger is pictured. Continuous motion of ion exchanger is facilitated with such columns. [Pg.69]

In a recent publication [646] concerning the same topic, the authors distinguished between the stirrer-controlled nd w 30 = const) and the gravity-controlled regime. However, a correlation of these data with the aid of Richardson number, Ri, see below, was not satisfactory. [Pg.111]

Figure 2 Placement of foaming-agent solution under gravity control as observed in sector Model 2 Injection from left to right through perforated lower 25% of wellbore height. Figure 2 Placement of foaming-agent solution under gravity control as observed in sector Model 2 Injection from left to right through perforated lower 25% of wellbore height.
R. Hashimoto, K. Yanagi, and T. Fujii, Effects of Condensate Flow Patterns upon Gravity-Controlled Condensation of Ethanol and Water Mixtures on a Vertical Surface, Heat Transfer-Japanese Research, 23, pp. 330-348,1994. [Pg.988]

Heat transfer coefficients for condensation processes depend on the condensation models involved, condensation rate, flow pattern, heat transfer surface geometry, and surface orientation. The behavior of condensate is controlled by inertia, gravity, vapor-liquid film interfacial shear, and surface tension forces. Two major condensation mechanisms in film condensation are gravity-controlled and shear-controlled (forced convective) condensation in passages where the surface tension effect is negligible. At high vapor shear, the condensate film may became turbulent. [Pg.1332]

Heat Transfer Correlations for External Condensation. Although the complexity of condensation heat transfer phenomena prevents a rigorous theoretical analysis, an external condensation for some simple situations and geometric configurations has been the subject of a mathematical modeling. The famous pioneering Nusselt theory of film condensation had led to a simple correlation for the determination of a heat transfer coefficient under conditions of gravity-controlled, laminar, wave-free condensation of a pure vapor on a vertical surface (either flat or tube). Modified versions of Nusselt s theory and further empirical studies have produced a list of many correlations, some of which are compiled in Table 17.23. [Pg.1332]

Film condensation in tube bundles (more commonly used in shell-and-tube heat exchangers) characterize more complex physical conditions compared to condensation on a single tube. The gravity-controlled and surface-shear-stress-influenced condensate films must be modeled in different ways to accommodate combined influences of condensate drain to lower tubes (i.e., condensate inundation) and shear effects. Such a correlation, the fourth correlation from the top of Table 17.24, was proposed by Kern and modified by Butterworth [81]. [Pg.1334]

Vertical Surfaces. If the laminar flow direction is downward and gravity-controlled, heat transfer coefficient for internal condensation inside vertical tubes can be predicted using the correlations for external film condensation—see Table 17.23. The condensation conditions usually occur under annular flow conditions. Discussion of modeling of the downward internal convective condensation is provided in Ref. 76. [Pg.1336]

A unique feature of the CGMDE is the possibility of automatic recalibration of the size of the electrode itself. From the process monitoring point of view, where the reproducibility of the experimental results is due to the advantage of automation - this aspect becomes especially significant. Here recalibration of the drop size can be achieved by generating the drop with a pulse sequence until it reaches the gravity controlled size. To make this problem more clear we shall discuss now the principle of recalibration as shown in Fig.3. [Pg.152]

Fig. II.6.2 Channel-flow system (a) with gravity-controlled solution flow from a reservoir, passing a reference electrode, flowing through a channel cell and a counter electrode, then passing through a capillary controlling the flow rate, and finally being collected. Rectangular channel cell corresponding to (a) with... Fig. II.6.2 Channel-flow system (a) with gravity-controlled solution flow from a reservoir, passing a reference electrode, flowing through a channel cell and a counter electrode, then passing through a capillary controlling the flow rate, and finally being collected. Rectangular channel cell corresponding to (a) with...
Row controller and/or gravity controller on the transfer pump discharge. [Pg.80]

Monitoring of battery facilities are conduced under the shift patrol by checking charge/discharge status, cell external conditions and specific gravity control. [Pg.168]

Determine if center of mass or center of gravity control is desired... [Pg.413]


See other pages where Gravity controller is mentioned: [Pg.567]    [Pg.1042]    [Pg.268]    [Pg.744]    [Pg.221]    [Pg.29]    [Pg.393]    [Pg.865]    [Pg.1339]    [Pg.1208]    [Pg.112]    [Pg.151]    [Pg.348]    [Pg.1334]    [Pg.1209]    [Pg.571]    [Pg.1046]    [Pg.12]    [Pg.149]    [Pg.153]    [Pg.859]    [Pg.1]    [Pg.470]    [Pg.216]    [Pg.161]    [Pg.170]    [Pg.1618]   
See also in sourсe #XX -- [ Pg.253 ]




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Sedimentation, gravity controls

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