A new strategy for the instrumental control of sample dispersion in continu
ous flow systems is presented. The method is based on shaking a loosely hel
d straight reactor while the sample travels through the flow injection mani
fold. This external disturbance yields a sample transport more similar to t
he plug flow type because of the changes promoted on the flow pattern. Up t
o a three-fold increase in peak height, a comparable reduction in peak widt
h and a more Gaussian peak profile are observed when the signals obtained w
ith the shaken reactor are compared with those obtained with the same react
or but static. Improvements in the analytical performance as a function of
different operational variables are shown for systems with or without a che
mical reaction. Analytical implications and possible uses are discussed sin
ce this strategy allows the control of dispersion by simply selecting the f
requency and amplitude of oscillation.