-We experimentally investigate hydrodynamic dispersion in elastic turbulent flows of a semi-dilute aqueous polymer solution within a periodic porous structure at ultra-low Reynolds numbers < 10 −3 by particle tracking velocimetry. Our results indicate that elastic turbulence can be characterized by an effective dispersion coefficient which exceeds that of Newtonian liquids by several orders of magnitude and grows non-linearly with the Weissenberg number Wi. Contrary to laminar flow conditions, the velocity field, and thus the shear rate, is not proportional to the flow rate and becomes asymmetric at high Wi.Introduction. -Turbulent flow is characterized by unsteady velocity fields which suddenly vary in space and time. For Newtonian liquids, this regime is reached for high Reynolds numbers Re, where inertial effects dominate over viscous forces. In contrast, for viscoelastic fluids, turbulent flow at arbitrarily small Re numbers, usually referred to as elastic turbulence [1], can be observed. Such fluids are characterized by an elastic response, e.g. due to the entanglement and the dynamics of polymer chains [2]. The degree of elastic effects can be described by the dimensionless Weissenberg number Wi = λ ·γ, which quantifies the anisotropic polymer alignment in the presence of shear [3]. Here, λ is the equilibrium polymer relaxation time andγ the shear rate of the flow. Accordingly, for Wi → 0 the response of the fluid to a sudden stress is purely viscous while for Wi > 0 an elastic short-time response is obtained. Since the polymer alignment not only depends on the instantaneous but also on the previous shear, this explains why a highly non-linear flow dependence on the shear strength is observed [2]. It has been experimentally demonstrated that above a critical Weissenberg number Wi c 1, elastic turbulence occurs [4]. Similar to inertial turbulence, this regime is characterized by an enhanced flow resistance and a power-law decay of the spectral power density [1,5,6]. This effect can be exploited to dramatically increase the mixing efficiency at small length scales and small Reynolds numbers (Re < 10 −4 ) in microfluidic devices [7,8].