A novel technique was used to fabricate nickel flow models of a straight pi
pe and a Y-bifurcation. These were used to obtain integral mass transfer co
efficients by the electrochemical technique. For the straight pipe, good ag
reement was obtained with previously reported mass transfer correlations. T
he use of an upstream anode in addition to the downstream anode led to high
er mass transfer at the cathode with laminar flow because of the additional
near-wall ions produced by the upstream anode. With increasing Schmidt num
ber, the effect of transition from laminar to turbulent flow on mass transf
er was delayed to progressively higher Reynolds numbers because of the redu
ced mass transfer boundary layer thickness relative to the viscous sublayer
. With the Y-bifurcation, possible flow separation and the formation of a n
ew mass transfer boundary layer in the daughter branches significantly infl
uence the mass transfer behaviour.