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BX gauze packings

The lowest resistance coefficients /fi are typical of stacked packing elements, honeycomb packings, tube columns as well as for type X packings made of sheet metal and type BX gauze packings with flow channels of 30°. They are in the range of /fi = 0.1—0.4. [Pg.75]

Hgim ftuS Wire-mesh structured packing . <0) Saber wire gauze packing BX (6) Sulzer wire gauze packing CY. IParta a and o, courtesy of Sober Chemteeh.)... [Pg.442]

The extraction column to be used in the process will have an internal gauze packing - Sulzer BX, that was chosen due to its large interfacial area, high porosity and low pressure drops. [Pg.489]

Type BX Metal gauze packing Rectification in vacuum starting at 1 mbar up to atmospheric pressure 0.9... [Pg.204]

Hiflow rings, structured Sulzer gauze packings (type BX), as well as type X sheet metal packings and Montz packings X with flow channels of a = 30° resulted in a higher flooding point constant Cfi,o. compared to Eq. (2-64), namely ... [Pg.76]

Further to the correlations presented above, there are a number of calculation examples at the end of this chapter, which illustrate how the model can be used to determine the vapour velocity at the flooding point for 50 mm randomly filled Pall rings for the system ethyl benzene/styrene under vacuum, and the gas velocity at the flooding point under pressure for 25 mm randomly filled Bialecki rings for the air/water system, for structured gauze packing BX as well as for 15 mm Pall rings made of plastic. [Pg.91]

Determining the vapour capacity factor Fv,fi> cc. to Eq. (2-67), for Sulzer gauze packing BX for the separation of the mixture ethyl benzene/styrene at a top pressure of 66.7 mbar. [Pg.95]

Fig. 3 8A. Heigjit of a mass transfer unit and pressure drop of Sulzer plastic gauze packing, type BX, versus the fector Fg for two different systems. Fig. 3 8A. Heigjit of a mass transfer unit and pressure drop of Sulzer plastic gauze packing, type BX, versus the fector Fg for two different systems.
Sulzer Gauze packing BX Plastic fibre gauze 500... [Pg.478]

Efficiency and pressure drop data for Siilzer BX metal gauze structured packing and for three test mixtures are shown in Fig. 14-7.5. For the ethyl benzene/styrene test mixture, the effect of operating pressure is shown. The high viscosity mixture, propylene glycoL/ethylene... [Pg.1400]

The hydraulic operation of structured packings with countercurrent gas and liquid flows is somewhat different than that of random dumped packings. The wire-gauze type is wetted by capillary action, so that the entire geometric surface area becomes available for mass transfer at low liquid flow rates. Thus, Sulzer BX packing was found to have 2 A times the static liquid holdup of Flexipac 2 or Gempak 2A sheet metal types of structured packings [14]. However, once the surface is completely wetted, capillary action has only a small effect as the liquid rate increases. [Pg.41]

See other pages where BX gauze packings is mentioned: [Pg.382]    [Pg.382]    [Pg.385]    [Pg.14]    [Pg.137]    [Pg.382]    [Pg.20]    [Pg.382]    [Pg.382]    [Pg.385]    [Pg.14]    [Pg.137]    [Pg.382]    [Pg.20]    [Pg.441]    [Pg.442]    [Pg.444]    [Pg.441]    [Pg.442]    [Pg.212]    [Pg.213]    [Pg.33]    [Pg.15]    [Pg.20]    [Pg.22]    [Pg.101]    [Pg.242]    [Pg.478]    [Pg.480]    [Pg.566]    [Pg.269]    [Pg.450]    [Pg.470]    [Pg.1062]    [Pg.295]    [Pg.450]    [Pg.295]    [Pg.588]    [Pg.40]    [Pg.295]   
See also in sourсe #XX -- [ Pg.75 ]



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