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Taylor flow liquid slug lengths

Berfif, G. Pintar, A., The role of gas bubbles and liquid slug lengths on mass transport in the Taylor flow through capillaries. Chem. Eng. Sci. 1997, 52 (21/22), 3709-3719. [Pg.164]

Bercic, G., Pintar, A. (1997). The role of gas bubbles and liquid slug lengths on mass transport in the Taylor flow through capillaries. Chemical Engineering Science, 52, 3709—3719. Beretta, A., Ferrari, P., Galbiati, L., Andreini, P. (1997). Horizontal oil-water flow in small diameter tubes. Flow patterns. International Communications in Heat and Mass Transfer, 24, 223-229. [Pg.43]

Liu, H., Vandu, C. O., Krishna, R. (2005). Hydrodynamics of Taylor flow in vertical capillaries How regimes, bubble rise velocity, liquid slug length, and pressure drop. Irulustrial and Engineering Chemistry Research, 44, 4884-4897. [Pg.92]

On the basis of the experimental studies of Taylor flow in capillaries of Heiszwolf et al. [48], an empirical correlation for estimating liquid slug lengths (ijiug) proposed by Kreutzer [30] ... [Pg.290]

Figure 9.9 Schematic of Taylor flow showing the definitions of the unit cell, gas bubble length Lb and the liquid slug length L,. The lengths of the nose L ose and tail L,aii sections of the gas bubble are also indicated. Mass transfer contributions in the Taylor flow are indicated with the numbers (i) bubble to wall through film, (2) bubble to slug, and (3) slug to wall. Figure 9.9 Schematic of Taylor flow showing the definitions of the unit cell, gas bubble length Lb and the liquid slug length L,. The lengths of the nose L ose and tail L,aii sections of the gas bubble are also indicated. Mass transfer contributions in the Taylor flow are indicated with the numbers (i) bubble to wall through film, (2) bubble to slug, and (3) slug to wall.
Figure 16 Relative increase of friction and mass transfer due to gas-liquid Taylor flow, compared to developed laminar flow in small tubes. represents the dimensionless length of a liquid slug. Re the Reynolds number based on the liquid. Figure 16 Relative increase of friction and mass transfer due to gas-liquid Taylor flow, compared to developed laminar flow in small tubes. represents the dimensionless length of a liquid slug. Re the Reynolds number based on the liquid.
Amador C, Salman W, Sanguanpiyapan S, Gavriilidis A, Angeli P (2004) Effect of gas/liquid inlet conditions on slug length in Taylor flow. In Proceedings 5th international conference on multiphase flow (CD-ROM), Japan... [Pg.3205]

C. Amador, W. Salman, S. Sanguanpiyapan, A. Gavriilidis, P. Angeli, Effect of gas/liquid inlet conditions on slug length in taylor flow, in Proceedings of the 5th International Conference of Multiphase Flow,... [Pg.244]


See other pages where Taylor flow liquid slug lengths is mentioned: [Pg.276]    [Pg.225]    [Pg.37]    [Pg.38]    [Pg.654]    [Pg.28]    [Pg.479]    [Pg.240]    [Pg.272]    [Pg.801]    [Pg.159]    [Pg.809]    [Pg.658]    [Pg.3202]    [Pg.3204]    [Pg.208]    [Pg.212]    [Pg.690]    [Pg.691]    [Pg.691]    [Pg.220]    [Pg.1974]    [Pg.1975]    [Pg.195]    [Pg.36]    [Pg.58]    [Pg.20]   
See also in sourсe #XX -- [ Pg.290 ]




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