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Flooding, column packed column

Fig. 24. Generalized method using log scales for estimating packed column flooding and pressure drop, AP, in kPa/m g = gravitational constant, 9.81 m/s t = kinematic viscosity in mm /s (= cSt) E, G have units of kg/(m s) are in kg/m and the packing factor, F, in can be found in... Fig. 24. Generalized method using log scales for estimating packed column flooding and pressure drop, AP, in kPa/m g = gravitational constant, 9.81 m/s t = kinematic viscosity in mm /s (= cSt) E, G have units of kg/(m s) are in kg/m and the packing factor, F, in can be found in...
Similar to tray columns, packed columns operated at high gas velocities causes backmixing, and low gas velocities reduce the mass transfer rate. If the gas velocity is too high, the column will flood. In addition, at low liquid flow rates the packing will not wet completely, resulting in a reduction in mass-transfer. Another problem is the tendency for the liquid to channel. To minimize this effect, redistributors have to be installed every 5 to 10 m (16.4 to 30.5 ft) [23] to even out the liquid flow. [Pg.327]

FIGURE 5.0-12 Eckert method Tor estimating packed column flooding and pressure drop (Ref. 20). (Now ... [Pg.307]

FIGURE 5,8-15 Design chart for packed column flooding. See Table 5,8-5 for factors of oilier packings. [Pg.313]

For total-reflux distillations carried out in packed columns, regions of loading and flooding are identified by their effects on mass-transfer efficiency, as shown in Fig. 14-47. Gas and liquid rate increase... [Pg.1387]

Flooding and Loading Since flooding or phase inversion normally represents the maximum capacity condition for a packed column, it is desirable to predict its value for new designs. The first generalized correlation of packed-column flood points was developed by Sherwood, Shipley, and Holloway [Ind. Eng. Chem., 30, 768 (1938)] on the basis of laboratory measurements primarily on the air-water system. [Pg.1387]

Calculation of column diameter (for packed columns, this is usually based on flooding conditions, and, for plate columns, on the optimum gas velocity or the liquid-handling capacity of the plate)... [Pg.2185]

The column must be flooded initially to wet the packing. For this reason it is customary to operate a still at reflux for some time before beginning the distillation. [Pg.10]

For column analysis and troubleshooting it is important to have pressure drop measured with a DP cell. The differential pressure can also be used to control column traffic. A good way to do this would be to let the differential pressure control the heating medium to the reboiler. The largest application for differential pressure control is with packed columns where it is desirable to run at 80 to 100% of flood for best efficiency. [Pg.69]

Strigle [94] proposed this term to better describe the performance of a packed column at or near the previously described loading point. Kister [93] evaluated the limited published data and proposed using the MOC at 95% of the flood point. The flood point can be estimated by Equation 9-20 or from the plots in References 90 and 93. The data are reported to be within 15-20% of the prediction [93]. See Figure 9-22 for the identification of MOC on the HETP vs. Cg chart For more accurate information... [Pg.299]

Packed columns can flood prematurely. Some of the reasons include ... [Pg.299]

A full discussion of flooding in packed columns is given in Volume 2, Chapter 4. [Pg.601]

The pressure drop through packed columns, and the flooding conditions, can be estimated from the generalized correlation of Leva (1992), shown in Fig. 13-5. The pressure gradient in millimeters of water per meter of packed height is the parameter on the curves, and interpolation is usually necessary to determine the pressure drop (note that the pressure... [Pg.400]

A packed column is used to scrub S02 from air by using water. The gas flow rate is 500 scfm/ft2, and the column operates at 90°F and 1 atm. If the column contains No. 1 plastic Intalox packing, what is the maximum liquid flow rate (per unit cross section of column) that could be used without flooding ... [Pg.410]

A column 0.6 m diameter and 4 m high is, packed with 25 mm ceramic Raschig rings and used in a gas absorption process carried out at 101.3 kN/m2 and 293 K. If the liquid and gas properties approximate to those of water and air respectively and their flowrates are 2.5 and 0.6 kg/m2s, what is the pressure drop across the column In making calculations, Carman s method should be used. By how much may the liquid flow rate be increased before the column floods ... [Pg.47]


See other pages where Flooding, column packed column is mentioned: [Pg.55]    [Pg.57]    [Pg.1555]    [Pg.1608]    [Pg.502]    [Pg.1551]    [Pg.1604]    [Pg.265]    [Pg.412]    [Pg.114]    [Pg.600]    [Pg.307]    [Pg.74]    [Pg.172]    [Pg.172]    [Pg.1386]    [Pg.1392]    [Pg.2115]    [Pg.2118]    [Pg.11]    [Pg.11]    [Pg.414]    [Pg.415]    [Pg.602]    [Pg.173]    [Pg.410]   
See also in sourсe #XX -- [ Pg.392 , Pg.393 , Pg.394 , Pg.395 , Pg.396 ]




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