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Impeller pumping number

The pumping number is a function of impeller type, the impeller/tank diameter ratio (D/T), and mixing Reynolds number Re = pND /p.. Figure 3 shows the relationship (2) for a 45° pitched blade turbine (PBT). The total flow in a mixing tank is the sum of the impeller flow and flow entrained by the hquid jet. The entrainment depends on the mixer geometry and impeller diameter. For large-size impellers, enhancement of total flow by entrainment is lower (Fig. 4) compared with small impellers. [Pg.420]

Impellers are sometimes viewed as pumping devices the total volumetric flow rate Q discharged by an impeller is made dimensionless in a pumping number ... [Pg.661]

Large tanks tend to develop a recirculation pattern from the impeller through the tank back to the impeller. This results in a behavior similar to that for a number of tanks in a series. The net result is that the mean circulation time is increased over what woiild be pre-dic ted from the impeller pumping capacity. This also increases the standard deviation of the circulation times around the mean. [Pg.1625]

Not only is the type of flow related to the impeller Reynolds number, but also such process performance characteristics as mixing time, impeller pumping rate, impeller power consumption, and heat- and mass-transfer coefficients can be correlated with this dimensionless group. [Pg.1629]

The primary pumping capacity of an impeller is determined by the impeller diameter, the Pumping number, and the rotational speed. The Pumping number Nq is defined by [13]... [Pg.576]

The Pumping number is used to determine the pumping rate Qp of an impeller,... [Pg.576]

Hicks et al. [8] developed a correlation involving the Pumping number and impeller Reynolds number for several ratios of impeller diameter to tank diameter (D /D ) for pitched-blade turbines. From this coiTclation, Qp can be determined, and thus the bulk fluid velocity from the cross-sectional area of the tank. The procedure for determining the parameters is iterative because the impeller diameter and rotational speed N appear in both dimensionless parameters (i.e., Npe and Nq). [Pg.576]

Figure 7-15 shows plots of Pumping number Nq and Power number Np as functions of Reynolds number Np for a pitched-blade turbine and high-efficiency impeller. Hicks et al. [8] further introduced the scale of agitation, S, as a measure for determining agitation intensity in pitched-blade impellers. The scale of agitation is based on a characteristic velocity, v, defined by... [Pg.576]

Figure 7-15. Power number and Pumping number as functions of Reynolds number for a pitched-blade turbine and high-efficiency impeller. (Source Bakker, A., and Gates L. , Properly Choose Mechanical Agitators for Viscous Liquids," Chem. Eng. Prog., pp. 25-34, 1995.)... Figure 7-15. Power number and Pumping number as functions of Reynolds number for a pitched-blade turbine and high-efficiency impeller. (Source Bakker, A., and Gates L. , Properly Choose Mechanical Agitators for Viscous Liquids," Chem. Eng. Prog., pp. 25-34, 1995.)...
Equation 13 is the empirical relationship obtained by the linear regression between D/T and terminal pumping numbers (4). It is important to note that a family of curves exists for each D/T ratio when Nq (pumping number) is plotted versus the impeller Reynolds number (5). In the turbulent range (iVRe > 2000), the Nq curves flatten out and thus are independent of the Reynolds number. [Pg.76]

Figure 1 Pumping number versus impeller Reynolds number for turbine and marine type propeller agitators. Figure 1 Pumping number versus impeller Reynolds number for turbine and marine type propeller agitators.
A 137.5-in-diameter tank has a cross-sectional area of (jr/4)(137.5 in)2 = 14,849 in2 or 103 ft2, so the required impeller pumping capacity is bulk velocity times cross-sectional area (0.4 ft/s)(103 ft2) = 41.2 ft3/s or 2472 ft3/min (1.17 m3/s). Geometry of the actual tank will be taken into consideration by location and number of impellers after the horsepower and speed of the agitator are determined. [Pg.441]

Select impeller diameter and determine required agitator speed. The pumping capacity Q for a pitched-blade impeller with four blades (NP = 1.37) can be related to other mixing parameters by the correlation shown in Fig. 12.3. The correlation is between two dimensionless variables pumping number (Q/ND3) and Reynolds number (D2NpIp.). Since impeller diameter D and rotational speed N appear in both variables, an iterative solution may be required. A convenient approach to such a solution is as follows ... [Pg.442]

FIGURE 12.3 Pumping number as a function of impeller Reynolds number for pitched-blade impeller (Np = 1.37). (From Chemical Engineering, 1976.)... [Pg.443]


See other pages where Impeller pumping number is mentioned: [Pg.389]    [Pg.389]    [Pg.426]    [Pg.447]    [Pg.465]    [Pg.36]    [Pg.773]    [Pg.96]    [Pg.47]    [Pg.63]    [Pg.288]    [Pg.447]    [Pg.465]    [Pg.443]    [Pg.285]    [Pg.296]    [Pg.302]    [Pg.687]    [Pg.687]    [Pg.739]   


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