Figure 2 shows gas bubbles and liquid in upwards co-current flow. Consider the plane A-A, drawn so that it lies entirely in the liquid. If Ul is the mean upwards liquid velocity across AA, continuity requires that:
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(4)
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This relation for the void fraction holds within certain limits for G and/or L negative - that is, for downflow of one or both phases.
Figure 2 Bubble flow.
Concerning the pressure gradient in the upwards vertical direction, note that the density of the liquid, which occupies a fraction (1-e) of the total volume, is much greater than that of the gas. Also, for the relatively low liquid velocities likely to be encountered in the bubble-flow regime, friction is negligible. Therefore, the pressure gradient is given fairy accurately by considering only the hydrostatic effect:
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