Two diffusion models have been developed to analyze gas transfer data
previously measured in an intravascular artificial lung consisting of
a central gas supply catheter from which are tethered a large number o
f blind-ended microporous fibers of equal length. A convective-diffusi
on model (CD) describes the countercurrent transfer of a binary gas pa
ir when gas is supplied at constant pressure conditions, and a well mi
xed (WM) cycled pressure model predicts transfer when the gas supply p
ressure is time cycled between compression and vacuum conditions. Regr
ession of gas to gas and liquid to gas excretion data with the CD mode
l resulted in estimates of the liquid phase mass transfer coefficient
k(Al). Because these values were intermediate between the k(Al) expect
ed for flow parallel to a cylinder and for flow normal to a cylinder,
gas transfer was influenced by both the tethered region of the fiber t
hat was nearly perpendicular to the axis of the test section and the f
ree end of the fiber that rested along the wall of the test section. W
ith a time cycled gas supply pressure, the enhanced carbon dioxide and
oxygen excretion predicted by the WM model was similar to the data, b
ut a loss in transfer efficiency with fiber length was not accounted f
or by the theory.